JPH0411832A - Bleaching of fish meat or the like with water and device therefor - Google Patents

Bleaching of fish meat or the like with water and device therefor

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Publication number
JPH0411832A
JPH0411832A JP11168490A JP11168490A JPH0411832A JP H0411832 A JPH0411832 A JP H0411832A JP 11168490 A JP11168490 A JP 11168490A JP 11168490 A JP11168490 A JP 11168490A JP H0411832 A JPH0411832 A JP H0411832A
Authority
JP
Japan
Prior art keywords
meat
water
fish
bleaching
fat
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
Application number
JP11168490A
Other languages
Japanese (ja)
Other versions
JPH0536005B2 (en
Inventor
Yasuo Kurihara
康夫 栗原
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.)
ZENKOKU KAMABOKO SUISAN KAKOUGIYOU KYODO KUMIAI RENGOKAI
Bibun Corp
Original Assignee
ZENKOKU KAMABOKO SUISAN KAKOUGIYOU KYODO KUMIAI RENGOKAI
Bibun 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 ZENKOKU KAMABOKO SUISAN KAKOUGIYOU KYODO KUMIAI RENGOKAI, Bibun Corp filed Critical ZENKOKU KAMABOKO SUISAN KAKOUGIYOU KYODO KUMIAI RENGOKAI
Priority to JP11168490A priority Critical patent/JPH0411832A/en
Publication of JPH0411832A publication Critical patent/JPH0411832A/en
Publication of JPH0536005B2 publication Critical patent/JPH0536005B2/ja
Granted legal-status Critical Current

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  • Processing Of Meat And Fish (AREA)

Abstract

PURPOSE:To prevent discharge of tasty components and nutritive components in raw material meat and to obtain high-quality meat bleached with water, suitable as a raw material for fish paste product, by adding bleaching water to picked meat, subjecting to reduced pressure to float and remove fats and then finely grinding the meat. CONSTITUTION:Picked meat of fresh fish or frozen fish is blended with preferably 3-10 times as much beaching water as the picked meat, subjected to reduced preferably under <=200Torr, floating fats are removed by scooping, etc., and then fine ground until thickness of fibers becomes 1-2mum to give the objective meat bleached with water.

Description

【発明の詳細な説明】[Detailed description of the invention] 【産業上の利用分野】[Industrial application field]

本発明は生鮮または冷凍魚等の落とし身から、高品質の
晒し肉を製造するための魚肉等の水晒し方法及び装置に
関するものである。
The present invention relates to a method and apparatus for bleaching fish meat, etc., for producing high quality bleached meat from fresh or frozen fish meat.

【従来の技術1 水産練製品における魚肉等の水晒しは、通常落とし身に
3〜5倍量の晒し用水を加えタンク内で攪拌してから回
転篩で予備脱水する操作を数回繰り返すことによって行
われている。 従来の方法では、その適用が生鮮魚の普通肉に限定され
るため、血合肉や冷凍魚の利用が殆どん図られていない
。とりわけマイワシをはじめとする赤身魚では、血合肉
や脂肪が多量に含まれることに加え、肉タンパク質自体
の不安定なことが、晒し肉の製造に大きな障害となって
いる。 【発明が解決しようとする課題】 本発明の目的は、上述の問題点を解決し、高品質の晒し
肉を製造可能にするために、生鮮または冷凍魚から得た
落とし身に晒し用水を加え200torr以下の減圧下
で、水晒し中に浮上する脂肪を除去しながら筋原繊維レ
ベルまで原料肉を微細化する水晒し方法及び装置を提供
することにある。 til1題を解決するための手段】 〔方法〕 生鮮魚または冷凍魚などから得た落とし身を、3〜10
倍量の晒し用水(肉質改良剤としてピロ又はトリポリリ
ン酸塩と重曹を添加すると共に、液温は10℃以下とす
ることが望ましい。)と混合し、200torr以下、
好ましくは5〜10torrの減圧下で、磨砕航に数分
程度脱気して、内申に含まれる空気と脂肪を水面へ浮上
させる。次いで浮上した脂肪を回収しながら、筋原繊維
レベル(繊維の太さ1〜2μm)まで原料肉をll11
11I化して水晒しを行う。200torr以下の減圧
下で水晒しを行うが、減圧度によってその時間は異なり
5〜10torrでは10〜20分が好適である。 水晒し中に浮上する脂肪の除去は、チャンバー内に設け
た反転ネットで掬い取る操作を繰り返すことによって行
う。 しかして水晒しの終わった微側化肉をII(ψII程度
が適当)で濾過し、夾雑する小骨、黒皮及び基質タンパ
ク質等を除去する。この後、濾液中の微細化肉を連続式
の遠心分離機によって脱水して回収し、晒し肉を得る。 〔装置〕 上述の方法を実施するために、減圧装置に連結され減圧
下に保持可能な一対の円筒容器の両端部を、略同径の接
続パイプと略同径を有しかつ脂肪回収用の反転ネットを
組み込んだチャンバーとで連結すると共に前記円筒容器
内には放射状に固定された整流板と原料肉の微細化兼移
送用の回転羽根とを交互に複数連設した魚肉等の水晒し
装置を使用する。 またこの水晒し装置は一対の円筒容器の下端部を接続パ
イプで連結し、これを水平から10〜50°立ち上げた
状態に形成すると共に該円筒容器の他端部ヘチャンバー
を垂直に連結することによって、減圧中に浮上する脂肪
やガスを効率良く水面へ浮上させることができる。 また水晒し装置の洗浄を容易にするために、チャンバー
全体を略水平状態まで反転可能にしである。 前記回転羽根の一側刃先部における断面は、原料肉を効
率良く微細化可能なように、円弧状(R状)に形成する
と共に他側部は、原料肉に上方又は下方に推力を付与す
るように上方または下方に勾配を設けて形成する。更に
推力の増大を図るためにこれらの回転羽根自体を若干の
勾配を設けた状態で円筒容器内に設置する。 またチャンバー上部には、エヤー抜き口、真空ポンプに
連結された減圧口及び原料投入口を、接続パイプ下部に
は、冷水供給口と原料排出口を夫々設ける。 以下、本発明装置による実施例を図面に従って説明する
。 まず原料魚をドレス又はフィレーとしてから、採肉機1
によって採肉し落とし身を得る。この落とし身を攪拌タ
ンク2内でピロリン酸塩等の肉質改良剤を含む晒し用水
と攪拌、混合した後、ポンプ4によって本発明装置へ供
給する。 本発明装置における一対の円筒状容器5・5の下端は、
円筒状容器5・5と略同径の接続バイブロで連結し、こ
れを水平から10〜50″立ち上げた状態に形成すると
共にその上端はチャンバー7の略同径の垂直部と連結さ
れる。そして下部接続バイブロにはバルブを有する冷水
供給口8と原料排出口9が、上部チャンバー7には、バ
ルブを有するエヤー抜きロ10.真空ポンプ13に連結
された減圧口11及び原料投入口12が夫々設けられて
いる。また前記チャンバー7は仕切板14によって原料
肉の減圧槽15と回収した脂肪のプール槽16に分割さ
れると共に減圧槽15には原料肉の循環を制御するため
の上部整流板17が設けられている。更にチャンバー7
には、油圧シリンダー18で駆動される浮上脂肪回収用
の反転ネット19が回動するように設けられており5チ
ヤンバー7の浮上脂肪を回収してプール槽16に分離し
、この分離時に反転ネット19に耐着、残存する脂肪は
プール槽16上に反転ネット19が回動された際、チャ
ンバ−7上部に設けたシャワー口20から散水により除
去するように構成されている。 また前記円筒状容器5・5内には、夫々モーター21で
駆動される回転軸22が軸支され、この回転軸22には
カラー23を介して適宜間隔をおいて複数の回転羽根2
4が取付けられると共に、この回転羽根24間には放射
状の整流板25が固定されていて複数の整流室26・2
6が上下方向に形成されている。 そして前記回転羽根24の刃先は、原料肉を効率良く微
細化可能なように円弧状(R状)24′に形成されると
共に他側部は、一方の円筒状容器5においては原料肉に
上方推力を、他方の円筒状容器51おいては原料肉に下
方推力を夫々付与するように、上方又は下方に勾配を設
けて形成される。更に推力の増大を図るためには回転羽
根24自体を、若干の勾配を設けた状態で回転軸22に
接合すると好適である6なお図中27は整流板25の固
定リング、28はチャンバー7の反転用の油圧シリンダ
ー、29は脂肪取出口、3oは原料排出口9にポンプを
介して連結される篩、31は遠心分離機、32は機台、
33はチャンバー7の覗き窓、34は肉質改良剤攪拌タ
ンクである。 従って本装置を200 torr以下、好ましくは5〜
10torr以下の減圧状態にして、原料投入口12か
らピロリン酸塩等の肉質改良剤を含む晒し用水と混合し
た原料肉を投入して脱気後、浮上した脂肪を反転ネット
19で回収しながら回転羽根24を駆動すると、回転羽
根24はその推力で原料肉を円筒状容器5・5内を夫々
上方又は下方に移送すると共に原料肉を微細化しながら
整流板25・25で乱流を生ずることなく移送され、更
に下部接続バイブロと上部チャンバー7を介して連続的
に循環移送されながら原料肉を筋原繊維レベルまで微細
化するものである。 これらの工程は減圧下で行われるため、原料肉の昇温か
かなり抑制され、原料肉の品質劣化(温度変性)を防止
できるので、冷却装置を特に必要としない6 また円筒状容器内の回転羽根間に設けた整流板により乱
流の発生を防止して原料肉を微細化しながら連続循環さ
せることが可能であるため、空気酸化による原料肉の品
質劣化を防止できる。 また減圧下で原料肉中の浮上する脂肪を効率良く分離除
去しながら原料肉を微細化するため薬剤の浸透性と臭気
成分の除去効果が高められる結果、ゲル形成能、脱脂及
び脱臭率に優れる高品質の晒し肉が製造できる。しかも
従来練製品原料として、弱足魚として位置づけられてき
たマイワシ等の赤身魚、特にこれらの冷凍魚からも末法
によって従来にない高品質の晒し肉が得られるので、今
後練製品原料の利用拡大を図ることもできる。 更には一回の水晒しによって晒し肉を製造するため、原
料肉中のアミノ酸等の呈味成分やビタミン等の栄養成分
等の流失を極力防止できると共に晒し液の排出処理の負
荷を軽減できる他、併せて装置自体の省スペース化と水
晒し工程の短縮化を図ることができる。 なお本工程はバッチ方式であるが、連続方式とすること
も可能である。 以下実施例により本発明の効果を更に具体的に説明する
。 なお下記実施例において、原料肉と晒し肉の分析項目及
び方法は次の通りである。 〔ゲル形成能〕 晒し肉の水分を84〜85%に調整し、食塩を3%添加
して10分間摺潰してからステンレス製容器(内径31
ma+、高さ30閣)に詰め密封した後、35℃で20
分間加熱してがら90’Cで20分間加熱してゲルを調
整した。 得られたゲルの強さは、第10図に示す大きさのピース
シニ切断してから引張り試験機で破断強度と破断伸びを
測定し、ゲル強度でゲルの強さを示した。更に噛み切り
試験(10点法で評価)と折り曲げ試験(−1±、十、
−の4段階で評価)でもゲルの強さを評価した。 〔色調〕 加熱ゲルの色調を、測色色差計によりL値とZ値から明
度とハンター白炭を夫々求めた。 〔−殻成分組成〕 常法によった6 (pH3 試料肉を10倍量の蒸留水と共にホモジナイズした後、
pHメーター(ガラス電極)により測定した。なおホモ
ジネートについてはそのまま測定した。 〔筋原繊維タンパク質の溶解度〕 0.05Mリン酸緩衝液(I=0.05、pH6,8)
に可溶な窒素を水溶性窒素とし、全タンパク質窒素を0
、IN NaOH可溶窒素と水溶性窒素の差から求めた
。 これとは別にO,,55MKCl−リン酸緩衝液(I 
=0.6、PH6,8)に可溶な窒素と水溶性窒素の差
から可溶性筋原繊維タンパク質窒素を求め、全筋原繊維
タンパク質窒素に対する割合をもって溶解度とした。 なお窒素の定量は、ケルゾール法によった。 〔回収した浮上脂肪〕 n−ヘキサン抽出法に準じて定量した。
[Conventional technology 1] Bleaching of fish meat, etc. in fish paste products is usually done by adding 3 to 5 times the amount of bleaching water to the dried fish, stirring it in a tank, and then pre-dehydrating it with a rotating sieve several times. It is being done. In the conventional method, the application is limited to normal meat of fresh fish, and therefore, the use of blood meat and frozen fish is hardly attempted. In particular, red fish such as sardines contain a large amount of blood and fat, and the instability of the meat protein itself is a major obstacle to producing bleached meat. [Problems to be Solved by the Invention] The purpose of the present invention is to solve the above-mentioned problems and to make it possible to produce high-quality bleached meat by adding bleaching water to drop meat obtained from fresh or frozen fish. It is an object of the present invention to provide a water bleaching method and apparatus for reducing raw meat to the level of myofibrils while removing fat that floats to the surface during water bleaching under reduced pressure of 200 torr or less. Method for solving til1 problem] [Method] Dose 3 to 10 pieces of minced meat obtained from fresh or frozen fish.
Mix it with twice the amount of bleaching water (it is desirable to add pyro or tripolyphosphate and baking soda as a meat quality improver, and keep the liquid temperature at 10°C or below), and add to the water at 200 torr or below.
Preferably, under a reduced pressure of 5 to 10 torr, deaeration is performed for several minutes during the grinding process to float the air and fat contained in the water to the surface of the water. Next, while collecting the floating fat, the raw meat was heated to the level of myofibrils (fiber thickness 1-2 μm).
11I and exposed to water. Water exposure is carried out under reduced pressure of 200 torr or less, and the time varies depending on the degree of reduced pressure, and at 5 to 10 torr, 10 to 20 minutes is suitable. The fat that floats to the surface during exposure to water is removed by repeating the scooping operation with an inverted net provided in the chamber. The microlateralized meat that has been exposed to water is then filtered through II (appropriately about ψII) to remove contaminating small bones, black skin, matrix proteins, and the like. Thereafter, the finely divided meat in the filtrate is dehydrated and recovered using a continuous centrifuge to obtain bleached meat. [Apparatus] In order to carry out the above method, both ends of a pair of cylindrical containers connected to a decompression device and capable of being maintained under reduced pressure are connected to a connecting pipe having approximately the same diameter and a tube for fat recovery. A water bleaching device for fish meat, etc., which is connected to a chamber incorporating an inversion net, and in which a plurality of rectifying plates fixed radially in the cylindrical container and rotating blades for micronizing and transporting the raw meat are arranged alternately. use. In addition, this water exposure device connects the lower ends of a pair of cylindrical containers with a connecting pipe so that they are raised 10 to 50 degrees from the horizontal, and vertically connects a chamber to the other end of the cylindrical containers. By doing so, fat and gas that float to the surface during decompression can be efficiently floated to the water surface. Furthermore, in order to facilitate cleaning of the water exposure device, the entire chamber can be turned over to a substantially horizontal position. The cross section of the cutting edge portion on one side of the rotary blade is formed in an arc shape (R shape) so that the raw material meat can be efficiently refined, and the other side portion applies thrust upward or downward to the raw material meat. It is formed with an upward or downward slope. Furthermore, in order to increase the thrust, these rotating blades themselves are installed in a cylindrical container with a slight slope. Further, an air vent, a decompression port connected to a vacuum pump, and a raw material input port are provided at the upper part of the chamber, and a cold water supply port and a raw material outlet are provided at the lower part of the connecting pipe. Embodiments of the apparatus of the present invention will be described below with reference to the drawings. First, the raw fish is dressed or filleted, then the meat harvesting machine 1
Harvest the meat and obtain the body. The dried meat is stirred and mixed with bleaching water containing a meat quality improver such as pyrophosphate in a stirring tank 2, and then supplied to the apparatus of the present invention by a pump 4. The lower ends of the pair of cylindrical containers 5, 5 in the device of the present invention are
It is connected to the cylindrical containers 5 and 5 by a connecting vibro having approximately the same diameter, and is raised up from the horizontal by 10 to 50 inches, and its upper end is connected to the vertical portion of the chamber 7 having approximately the same diameter. The lower connected vibro has a cold water supply port 8 with a valve and a raw material outlet 9, and the upper chamber 7 has an air vent 10 with a valve, a decompression port 11 connected to a vacuum pump 13, and a raw material input port 12. The chamber 7 is divided by a partition plate 14 into a reduced pressure tank 15 for raw meat and a pool tank 16 for recovered fat, and the reduced pressure tank 15 has an upper rectifier for controlling the circulation of raw meat. A plate 17 is provided.Furthermore, a chamber 7 is provided.
A reversing net 19 for recovering floating fat, which is driven by a hydraulic cylinder 18, is rotatably installed, and the floating fat in five chambers 7 is collected and separated into a pool tank 16, and during this separation, the reversing net 19 is rotated. When the reversing net 19 is rotated over the pool tank 16, the remaining fat is removed by sprinkling water from the shower port 20 provided at the top of the chamber 7. Further, a rotating shaft 22 driven by a motor 21 is supported in each of the cylindrical containers 5, 5, and a plurality of rotating blades 2 are mounted on the rotating shaft 22 at appropriate intervals via a collar 23.
4 is attached, and a radial rectifying plate 25 is fixed between the rotary blades 24 to form a plurality of rectifying chambers 26 and 2.
6 are formed in the vertical direction. The cutting edge of the rotary blade 24 is formed into an arc shape (R-shape) 24' so that the raw material meat can be efficiently finely divided, and the other side portion is formed in an upward direction toward the raw material meat in one cylindrical container 5. The other cylindrical container 51 is formed with an upward or downward slope so as to apply a downward thrust to the raw meat in the other cylindrical container 51. In order to further increase the thrust, it is preferable to connect the rotating blade 24 itself to the rotating shaft 22 with a slight slope. A hydraulic cylinder for reversal, 29 a fat extraction port, 3o a sieve connected to the raw material discharge port 9 via a pump, 31 a centrifugal separator, 32 a machine stand,
33 is a viewing window of the chamber 7, and 34 is a meat quality improver stirring tank. Therefore, this device should be operated at a pressure of 200 torr or less, preferably 5 to
Under reduced pressure of 10 torr or less, raw meat mixed with bleaching water containing a meat quality improver such as pyrophosphate is introduced from the raw material input port 12, and after degassing, the fat that floats to the surface is collected by an inversion net 19 and rotated. When the blades 24 are driven, the rotary blades 24 use their thrust to transport the raw meat upwards or downwards inside the cylindrical containers 5, 5, respectively, and while pulverizing the raw meat, the current plates 25, 25 prevent turbulence from occurring. The raw meat is transported and further circulated continuously through the lower connecting vibro and the upper chamber 7 to refine the raw meat to the level of myofibrils. Since these processes are carried out under reduced pressure, the temperature rise of the raw meat is considerably suppressed, and quality deterioration (temperature denaturation) of the raw meat can be prevented, so there is no particular need for a cooling device6. Since it is possible to continuously circulate the raw meat while making it finer by preventing the generation of turbulence by using the baffle plate provided between them, it is possible to prevent quality deterioration of the raw meat due to air oxidation. In addition, by efficiently separating and removing the floating fat in raw meat under reduced pressure and making the raw meat finer, the permeability of chemicals and the removal effect of odor components are enhanced, resulting in excellent gel-forming ability, degreasing, and deodorizing efficiency. High quality bleached meat can be produced. In addition, red fish such as sardines, which have traditionally been regarded as weak-legged fish, and especially frozen fish, can be used as raw materials for paste products to obtain high-quality bleached meat that has never been available before, so the use of raw materials for paste products will expand in the future. It is also possible to aim for Furthermore, since bleached meat is produced by one-time water bleaching, it is possible to prevent the loss of flavor components such as amino acids and nutritional components such as vitamins in the raw meat as much as possible, and to reduce the burden of discharging the bleaching solution. At the same time, the space of the device itself can be saved and the water exposure process can be shortened. Although this process is a batch method, it is also possible to use a continuous method. The effects of the present invention will be explained in more detail with reference to Examples below. In the examples below, the analysis items and methods for raw meat and bleached meat are as follows. [Gel-forming ability] Adjust the moisture content of the bleached meat to 84-85%, add 3% salt, grind for 10 minutes, and then place in a stainless steel container (inner diameter 31
After being packed and sealed in a container (ma+, height 30 cm), it was heated at 35℃ for 20 minutes.
The gel was prepared by heating at 90'C for 20 minutes with heating for 20 minutes. The strength of the obtained gel was determined by cutting it into pieces having the size shown in FIG. 10 and measuring the breaking strength and breaking elongation using a tensile tester, and the gel strength was expressed as the gel strength. Furthermore, the bite test (evaluated using a 10-point scale) and the bending test (-1±, 10,
The strength of the gel was also evaluated on a 4-level scale (-). [Color tone] The color tone of the heated gel was determined by the lightness and Hunter white charcoal from the L value and Z value using a colorimeter. [-Shell component composition] After homogenizing the sample meat with 10 times the volume of distilled water,
Measured with a pH meter (glass electrode). Note that the homogenate was measured as it was. [Solubility of myofibrillar protein] 0.05M phosphate buffer (I=0.05, pH 6,8)
The nitrogen soluble in
, IN It was determined from the difference between NaOH-soluble nitrogen and water-soluble nitrogen. Separately, O, 55M KCl-phosphate buffer (I
Soluble myofibrillar protein nitrogen was determined from the difference between nitrogen soluble at pH 6,8) and water-soluble nitrogen, and the solubility was defined as the ratio to the total myofibrillar protein nitrogen. Note that nitrogen was determined by the Kelsol method. [Recovered floating fat] It was quantified according to the n-hexane extraction method.

【実施例11 マイワシ冷凍魚を原料として、−25℃での貯蔵期間が
1力月目と2力月目の2回にわたって、磨砕期間を変え
て得られる晒し肉の品質を調べた。 血合肉を含めた精肉を採肉機によって採取し。 重曹とピロリン酸塩を含む晒し用水と混合してから1本
水晒し装置へ投入後、真空度が10torrに達してか
ら所定の時間磨砕してホモジネートの一部を採取する操
作を繰り返した。磨砕時間の長短により、原料肉(特に
血合肉)の微細化の程度に違いのあることから、濾過操
作を省いて採取したホモジネートをそのまま遠心脱水し
た。 得られた晒し肉の水分を84〜85%に調整し。 のゲル形成能と筋原繊維タンパク質の溶解性を調べた。 まず、磨砕中の真空度、液温及びPHの変化を第12図
と第13@に示す。真空度は1@目の試験(磨砕時間2
0分まで)では、磨砕終了直前の測定値のみ、2回目の
試験(磨砕時間50分まで)では、その他の磨砕開始直
後の真空度も示した。磨砕中やや真空度が減少した1回
目と、特に30分以後これとは逆に真空度が上昇した2
回目とは傾向がやや異なるが、全試験区を通じ1310
torr以下で磨砕を行うことができた。傾向が異なる
のは磨砕時間の長さの他に真空ポンプの能力とのバラン
ス、装置の気密性、外気温や液温等が影響しているもの
と考えられる。ちなみに外気温は1回目で2.4℃、2
回目で10.4℃であった。 液温は2回の試験とも磨砕時間が長くなるに従って徐々
に上昇した。しかし1分当りの上昇温度を算出すると1
回目約0.15℃、2回目約0.13℃で、常圧磨砕の
場合の上昇温度約0.7℃と比較すると、減圧すること
で温度の上昇をかなり抑制できることが明らかになった
。 次に以上の条件下で得られた晒し肉の品質について調べ
た結果を、夫々第14図と第15図及び第16図と第1
7図に示す。ゲルの強さと筋原繊維タンパク質の溶解性
はともに、10〜20分まで上昇してから平行に達し、
その後徐々に低下した6しかしながら50分磨砕区の晒
し肉から調整したゲルでも折り曲げ試験でひびも入らず
、噛み切り試験で5〜6点の成績が得らており、減圧磨
砕の有効性が認められた。 【実施例2】 一25℃で2力月間貯蔵したマイワシを原料とし、水晒
し中に浮上する脂肪の除去の有無が晒し肉の品質に及ぼ
す影響を調べた。 まずホモジネートの脂肪含量について調べた結果を表1
に示す。脂肪含量を乾燥量基準で比較すると、非除去区
では除去区より約2.4倍高い数値を示した。 次に篩で夾雑物を除去した晒し肉のゲル形成能とゲルの
色調を調べた結果を表2に示す。 表2.′4上脂肪除去の有無が晒し肉の品質に晒し肉の
pHは両区とも7.14であったが、摺潰時に添加する
食塩の影響で、PHが0.2〜0.3低下することから
、タリンサン(ピロリン酸塩とトリポリリン酸塩の等景
況合物)を0.2%添加することで。 PHの低下を補正したゲルを調整した。 ゲルの強さについては除去区の方が非除去区よりやや優
れていたが、破断強度、破断伸びともにかなり高い数値
が得られており、特に破断伸びの改善が著しくその数値
は3以上となっており、エソ、グチ等の強足魚のそれと
同レベルに達している。 ゲルの色調については除去区と非除去区で大差なかった
[Example 11] Using frozen sardine fish as a raw material, the quality of bleached meat obtained by changing the grinding period was examined over two storage periods at -25°C, the first and second months. The meat, including blood meat, is collected using a meat harvesting machine. After mixing with bleaching water containing baking soda and pyrophosphate, one bottle was put into a water bleaching device, and after the degree of vacuum reached 10 torr, the operation of grinding for a predetermined time and collecting a part of the homogenate was repeated. Since the degree of fineness of the raw meat (particularly blood meat) varies depending on the length of the grinding time, the homogenate collected without the filtration operation was directly centrifugally dehydrated. The moisture content of the obtained bleached meat was adjusted to 84-85%. The gel-forming ability and solubility of myofibrillar proteins were investigated. First, changes in the degree of vacuum, liquid temperature, and pH during grinding are shown in Figures 12 and 13@. The degree of vacuum is the 1st test (grinding time 2)
In the second test (up to 50 minutes of grinding time), only the measured value immediately before the end of grinding was shown, and in the second test (up to 50 minutes of grinding time), other vacuum degrees were also shown immediately after the start of grinding. The first time the degree of vacuum decreased slightly during grinding, and the second time the degree of vacuum increased, especially after 30 minutes.
Although the trend is slightly different from the first time, it was 1310 in all test areas.
Grinding could be performed at torr or less. The difference in trends is thought to be due to factors such as the length of the grinding time, the balance with the capacity of the vacuum pump, the airtightness of the device, the outside air temperature, and the liquid temperature. By the way, the outside temperature was 2.4℃, 2.
The temperature was 10.4°C. The liquid temperature gradually increased as the grinding time increased in both tests. However, when calculating the temperature rise per minute, it is 1
The temperature rise was approximately 0.15°C for the first time and approximately 0.13°C for the second time, which was approximately 0.7°C in the case of normal pressure grinding, and it became clear that the temperature rise could be significantly suppressed by reducing the pressure. . Next, the results of examining the quality of the bleached meat obtained under the above conditions are shown in Figures 14 and 15, Figures 16 and 1, respectively.
It is shown in Figure 7. Both gel strength and myofibrillar protein solubility increase until 10-20 minutes before reaching a parallel level.
However, the gel prepared from the bleached meat after 50 minutes of grinding showed no cracks in the bending test, and a score of 5 to 6 was obtained in the bite test, demonstrating the effectiveness of vacuum grinding. was recognized. [Example 2] Using sardines stored at -25°C for 2 months as a raw material, the effect of whether or not the fat that floats to the surface during bleaching in water is removed on the quality of the bleached meat was investigated. First, we investigated the fat content of the homogenate, and the results are shown in Table 1.
Shown below. When the fat content was compared on a dry basis, the non-removed area showed a value about 2.4 times higher than the removed area. Next, the gel-forming ability and color tone of the bleached meat from which impurities were removed using a sieve were examined, and the results are shown in Table 2. Table 2. '4 The pH of the bleached meat was 7.14 in both groups, but the pH decreased by 0.2 to 0.3 due to the influence of the salt added during grinding. Therefore, by adding 0.2% of talinsan (equal composition of pyrophosphate and tripolyphosphate). A gel was prepared that corrected for the decrease in pH. In terms of gel strength, the gel strength in the removed area was slightly better than in the non-removed area, but significantly higher values were obtained for both breaking strength and elongation at break, with the improvement in elongation at break being particularly marked, reaching values of 3 or higher. It has reached the same level as that of strong-legged fish such as Eso and Japanese croaker. There was no significant difference in gel color between the removed and non-removed areas.

【実施例3】 一25℃での貯蔵期間が1又は2力月のマイワシ冷凍魚
を原料として、水接によって製造した晒し肉の一般成分
組成を表3に、また落とし身(原料肉)のそれを表4に
示す。 落とし身の成分組成は原料魚によって異なり、特に水分
と脂肪含量に違いがみられた。 一方、晒し肉の成分組成は、おおむね一定していたが詳
細に検討すると、製造方法の違いによる差異がみられた
。例えば3月6日の上3例と下3例は浮上脂肪の除去を
行った場合と行わなかった場合の結果で、後者の方が0
.2%粗脂肪含量が高かった。いいずれにしても粗脂肪
含量は1%以下になっており、品質に悪影響を与える脂
肪変敗を少なくする点で、冷凍すり身の品質向上に貢献
するものと思われる。 9唯1月31日 3  7.28  羽、2−0.8−
2月1日 3  7.32 84.4 −   0.7
 −2月1日 5  7.37 85.5 −   0
.7 −3月5日 3  7.12 81.7 17.
1  0.7 0.3    2203月5日 3月6日 3月6日 3月6日 3月6日 3月6日 3月6日 長崎 3月7日 3月7日 3月8日 7.12 7【4 82.4 81.6 81.7 82.0 81.7 81.6 81.8 82.6 81.6 80.5 17.3 17.2 17.1 17.5 17.3 17.2 17.3 17.0 17.5 17.8 0.5 0.3 0.7 0.4 0.9 0.4 0.7 0.7 0.4 表4.落と 第9図は第2図C−C線断面図、第10図は本発明で得
られたゲルの強さを測定するためのピースの正面図、第
11図は第2図C−C線断面図。 第12図乃至第17図は夫々本発明の品質説明図である
。 1・・・円筒状容器、6・・・接続パイプ、7・・・チ
ャンバー、13・・・真空ポンプ、19・・・反転ネッ
ト、24・・・回転羽根、25・・・整流板。 境港 鱗1月31日 70.1  18.9    7
.8  1.2   4872月1日 71.0  1
g、4     g、2  1.2   3883月5
日 72,5  18.2    8.8  1.2 
  4643月6日 73,9  18.0    7
.8  1.1長崎    3月7日 酩、0  20
.2    13.6  1.2   4823月8日
 釘、8  19.9    13.3  1.1特許
出願人  株式会社備文機械製作所  外1名
[Example 3] Table 3 shows the general composition of bleached meat produced by water wetting using frozen sardine fish that has been stored for 1 or 2 months at -25°C. It is shown in Table 4. The composition of ochimi differs depending on the raw fish, especially in water and fat content. On the other hand, the composition of bleached meat was generally constant, but upon closer examination, differences were found due to differences in the manufacturing method. For example, the top three cases and bottom three cases on March 6th show the results when floating fat was removed and when the floating fat was not removed, and the latter was 0%.
.. 2% crude fat content was high. In any case, the crude fat content is 1% or less, which is thought to contribute to improving the quality of frozen surimi by reducing fat spoilage that adversely affects quality. 9 only January 31st 3 7.28 birds, 2-0.8-
February 1st 3 7.32 84.4 - 0.7
-February 1st 5 7.37 85.5 - 0
.. 7 - March 5th 3 7.12 81.7 17.
1 0.7 0.3 220 March 5 March 6 March 6 March 6 March 6 March 6 March 6 Nagasaki March 7 March 7 March 8 7. 12 7 [4 82.4 81.6 81.7 82.0 81.7 81.6 81.8 82.6 81.6 80.5 17.3 17.2 17.1 17.5 17.3 17 .2 17.3 17.0 17.5 17.8 0.5 0.3 0.7 0.4 0.9 0.4 0.7 0.7 0.4 Table 4. Figure 9 is a sectional view taken along the line C-C in Figure 2, Figure 10 is a front view of a piece for measuring the strength of the gel obtained by the present invention, and Figure 11 is a cross-sectional view taken along the line CC in Figure 2. Cross-sectional view. FIG. 12 to FIG. 17 are diagrams each illustrating the quality of the present invention. DESCRIPTION OF SYMBOLS 1... Cylindrical container, 6... Connection pipe, 7... Chamber, 13... Vacuum pump, 19... Reversing net, 24... Rotating vane, 25... Current plate. Sakaiminato Scale January 31st 70.1 18.9 7
.. 8 1.2 487February 1st 71.0 1
g, 4 g, 2 1.2 388 March 5
Sun 72.5 18.2 8.8 1.2
464March 6th 73,9 18.0 7
.. 8 1.1 Nagasaki March 7th Drunk, 0 20
.. 2 13.6 1.2 482 March 8 Nail, 8 19.9 13.3 1.1 Patent applicant Bibun Kikai Seisakusho Co., Ltd. and 1 other person

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の縦断正面図、第2図は同要部の縦断正
面図、第3図は同要部の平面図、第4図は同要部の側面
図、第5図は第2図C−C線断面図、第6図は回転羽根
の平面図、−第7図は第2図C−C線断面図、第8図は
第2図C−C線断面図、第3図 第S図 第 図 第 ′1 −21: 第4図 第8 図 平成 月   日
Fig. 1 is a longitudinal sectional front view of the present invention, Fig. 2 is a longitudinal sectional front view of the main parts, Fig. 3 is a plan view of the main parts, Fig. 4 is a side view of the main parts, and Fig. 5 is a longitudinal sectional front view of the main parts. Figure 2 is a sectional view taken along the line CC, Figure 6 is a plan view of the rotating blade, - Figure 7 is a sectional view taken along the line CC of Figure 2, Figure 8 is a sectional view taken along the line CC of Figure 2, and Figure 3 is a sectional view taken along the line CC of Figure 2. Figure S Figure '1-21: Figure 4 Figure 8 Figure 8

Claims (1)

【特許請求の範囲】 1、生鮮または冷凍魚等から得た落とし身に、晒し用水
を加えて減圧下で水晒しすると共に浮上する脂肪を回収
しながら筋原繊維レベルまで原料肉を微細化することを
特徴とする魚肉等の水晒し方法。 2、減圧下に保持可能な一対の円筒容器の両端部を、各
々略同径の接続パイプと脂肪回収用の反転ネットを組み
込んだチャンバーで夫々連結すると共に、前記円筒容器
内に放射状に固定された整流板と原料肉の微細化兼移送
用の回転羽根とを交互に複数連設したことを特徴とする
魚肉等の水晒し装置。 3、一対の円筒容器の下端部を接続パイプで連結し、こ
れを水平から10〜50゜立ち上げた状態に形成し、該
円筒容器の上端部にチャンバーを垂直状に連結した請求
項2記載の魚肉等の水晒し装置。
[Claims] 1. Bleaching water is added to drop meat obtained from fresh or frozen fish, etc., and the raw meat is refined to the level of myofibrils while being exposed to water under reduced pressure and recovering the fat that floats to the surface. A method for exposing fish meat, etc. to water, which is characterized by: 2. Both ends of a pair of cylindrical containers that can be maintained under reduced pressure are connected by a chamber incorporating a connecting pipe of approximately the same diameter and an inversion net for fat recovery, and fixed radially within the cylindrical container. A water bleaching device for fish meat, etc., characterized in that a plurality of rectifier plates and rotary blades for refining and transporting raw meat are arranged alternately in series. 3. The lower ends of the pair of cylindrical containers are connected by a connecting pipe, which are raised up from the horizontal by 10 to 50 degrees, and the chamber is vertically connected to the upper end of the cylindrical containers. Water bleaching equipment for fish meat, etc.
JP11168490A 1990-05-01 1990-05-01 Bleaching of fish meat or the like with water and device therefor Granted JPH0411832A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11168490A JPH0411832A (en) 1990-05-01 1990-05-01 Bleaching of fish meat or the like with water and device therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11168490A JPH0411832A (en) 1990-05-01 1990-05-01 Bleaching of fish meat or the like with water and device therefor

Publications (2)

Publication Number Publication Date
JPH0411832A true JPH0411832A (en) 1992-01-16
JPH0536005B2 JPH0536005B2 (en) 1993-05-28

Family

ID=14567560

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11168490A Granted JPH0411832A (en) 1990-05-01 1990-05-01 Bleaching of fish meat or the like with water and device therefor

Country Status (1)

Country Link
JP (1) JPH0411832A (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01222761A (en) * 1988-03-02 1989-09-06 Toukaiku Suisan Kenkyu Shocho Preparation of blanched meat

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01222761A (en) * 1988-03-02 1989-09-06 Toukaiku Suisan Kenkyu Shocho Preparation of blanched meat

Also Published As

Publication number Publication date
JPH0536005B2 (en) 1993-05-28

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