JP2545330B2 - Reprocessing method of seasoning liquid waste - Google Patents

Reprocessing method of seasoning liquid waste

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Publication number
JP2545330B2
JP2545330B2 JP5187401A JP18740193A JP2545330B2 JP 2545330 B2 JP2545330 B2 JP 2545330B2 JP 5187401 A JP5187401 A JP 5187401A JP 18740193 A JP18740193 A JP 18740193A JP 2545330 B2 JP2545330 B2 JP 2545330B2
Authority
JP
Japan
Prior art keywords
liquid
seasoning liquid
seasoning
waste
waste liquid
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 - Fee Related
Application number
JP5187401A
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Japanese (ja)
Other versions
JPH0716073A (en
Inventor
健一 田中
正彦 国本
伸雄 篠原
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.)
TANAKA SHOYU JOZOJO JUGEN
YAMAGUCHIKEN
Original Assignee
TANAKA SHOYU JOZOJO JUGEN
YAMAGUCHIKEN
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Priority to JP5187401A priority Critical patent/JP2545330B2/en
Publication of JPH0716073A publication Critical patent/JPH0716073A/en
Application granted granted Critical
Publication of JP2545330B2 publication Critical patent/JP2545330B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は調味液廃液の再生処理方
法に関し,特に水産物を調味液に浸漬して味付けする漬
け込み工程後に生じる調味液廃液の再生処理方法に関す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for regenerating a seasoning liquid waste liquid, and more particularly to a method for regenerating a seasoning liquid waste liquid generated after a dipping process in which a marine product is dipped in a seasoning liquid and seasoned.

【0002】[0002]

【従来の技術及び発明が解決しようとする課題】周知の
ごとく,水産物を調味液に浸漬して味付けする漬け込み
工程後に生じる調味液は,従来は廃棄するために排水処
理されているが,その有機物濃度が著しく高いため,排
水処理施設への負荷が大きくなり,施設の管理運転に多
大な費用を要することが問題となっている。上記漬け込
み工程後の調味液廃液には,従来以下の理由により利用
価値のない廃液として廃棄されている。 (1)漬け込みにより魚からエキス及び脂質等が調味液
中へ溶出するため,その調味液廃液は強い魚臭を発生す
る。(2)魚に由来する皮,肉片及び粘膜等の夾雑物を
多量に含んでいるため,この漬け込み工程後の調味液廃
液を再度水産物の漬け込み用調味液として使用した場合
は,それら夾雑物が製品に付着して外観及び風味を著し
く低下させる。(3)同様に魚からゼラチン等の水溶性
蛋白質が溶出し,調味液の粘度が上昇すると共に,脂質
が乳化して液が著しく混濁し,この液を再度水産物漬け
込み用調味液として使用した場合は,光沢が悪く,漬け
込みに長時間を要する。(4)原料魚に由来する水分の
ため調味液が2倍程度に希釈され,また腐敗し易い。 以上の欠点のために,漬け込み工程後の調味液廃液は,
利用価値のないものとして廃棄されており,その公害排
水処理に多大な費用を要することが問題となっている。
そこで,本発明者は前記課題を解決すべく種々研究の結
果,従来廃棄されていた調味液廃液を再生して良品質の
漬け込み用調味液を取得する再生処理方法を開発した。
2. Description of the Related Art As is well known, the seasoning liquid produced after the soaking process of dipping marine products in seasoning liquid for seasoning is conventionally treated as waste water for disposal, but the organic matter Since the concentration is remarkably high, the load on the wastewater treatment facility becomes large, and the management operation of the facility requires a great deal of cost. The seasoning liquid waste liquid after the pickling process is conventionally discarded as a waste liquid having no utility value for the following reasons. (1) Extracts, lipids, etc. are eluted from the fish into the seasoning liquid by pickling, and the waste liquid of the seasoning liquid produces a strong fish odor. (2) Since it contains a large amount of contaminants such as skins, meat pieces, and mucous membranes derived from fish, when the seasoning liquid waste solution after this pickling process is used again as a seasoning liquid for pickling marine products, those impurities are It adheres to the product and significantly reduces the appearance and flavor. (3) Similarly, when water-soluble proteins such as gelatin are eluted from fish and the viscosity of the seasoning liquid increases, lipids are emulsified and the liquid becomes extremely cloudy. When this liquid is used again as a seasoning liquid for pickling marine products Has a low gloss and requires a long time for pickling. (4) Due to the water content of the raw material fish, the seasoning liquid is diluted about twice and is also prone to putrefaction. Due to the above drawbacks, the seasoning liquid waste liquid after the pickling process is
The problem is that the waste is disposed of as being of no use value, and the treatment of the pollution wastewater requires a great deal of money.
Therefore, as a result of various studies to solve the above problems, the present inventor has developed a regeneration treatment method of regenerating the seasoning liquid waste liquid which has been conventionally discarded to obtain a good quality seasoning liquid for soaking.

【0003】[0003]

【課題を解決するための手段及び作用】本発明の上記課
題の解決は,以下の手段によって達成される。 (1)水産物を調味液に浸漬して味付けする漬け込み工
程後に生じる糖度が20〜40%の調味液廃液へ,麹菌
由来のプロテアーゼを0.05〜0.5%となるように
添加し,酵素反応温度40〜60℃,反応時間2〜48
時間で酵素反応を行わせながら糖度30〜60%まで減
圧蒸留濃縮後,▲ろ▼過又は遠心分離後▲ろ▼過して再
生調味液を取得することを特徴とする調味液廃液の再生
処理方法。 (2)遠心分離の回転数が,5,000〜20,000
回転/分であることを特徴とする前記(1)項記載の調
味液廃液の再生処理方法。 (3)▲ろ▼過が,精密▲ろ▼過であることを特徴とす
る前記(1)項記載の調味液廃液の再生処理方法。
Means and Actions for Solving the Problems The above-mentioned problems of the present invention can be solved by the following means. (1) Add the protease derived from Aspergillus oryzae to 0.05 to 0.5% to the waste liquid of the seasoning liquid having a sugar content of 20 to 40%, which is produced after the soaking process in which the marine product is soaked in the seasoning liquid to season the enzyme. Reaction temperature 40-60 ° C, reaction time 2-48
Regeneration treatment of seasoning liquid waste, characterized in that regenerated seasoning liquid is obtained by concentrating under reduced pressure to a sugar content of 30 to 60% under reduced pressure while performing an enzymatic reaction over time, and then filtering or centrifuging. Method. (2) The rotation speed of centrifugation is 5,000 to 20,000.
The method for regenerating a seasoning liquid waste according to the above item (1), wherein the method is a rotation / minute. (3) The method for regenerating a seasoning liquid waste according to (1) above, wherein the filtration is a precision filtration.

【0004】水産物へ用いる調味液は,濃口醤油へ砂
糖,水アメ等の糖類及びアミノ酸等の添加物を混合する
ことによって,糖度が45〜55%の濃度となるように
調製されている。さらに,これら調味液は漬け込み後,
原料魚からの脱水作用により,糖度が25%前後に希釈
され,かつ魚臭が強い、溶出蛋白質の多い廃液となる。
したがってこの調味液廃液の再生については、これらの
溶出成分の分解可溶化が必要となる。廃液中のこれらの
蛋白質を分解するためには、酵素剤の使用が望ましい。
この場合廃液は醤油が主成分であるため、pHが4.5
〜5.0の範囲にある。このような低いpH域の廃液分
解に適した酵素剤としては、麹菌由来のプロテアーゼが
適している。本発明では溶出蛋白質を効果的に分解する
ために、幅広い基質特異性を持ち、かつエキソペプチダ
ーゼとエンドペプチダーゼ活性を有する市販の酵素剤を
選択した。また魚臭の原因となる脂質の分解除去につい
ては、プロテアーゼの作用によって、一部分解されるも
のの十分ではないため、精密ろ過膜を使用して濾過する
ことによって解決した。ここで廃液中の凝固物の濾過法
において,大きなものの除去は遠心分離法により、小さ
なものは精密ろ過膜法にしたがって行った。本発明で用
いる精密濾過膜では、精密ろ過膜を用いることにより
0.1ミクロン以上の微粒子を除去することができ,そ
の結果廃液中の魚臭が効果的に消失することを見いだし
た。また濾過法の中に一般的な濾過方法である濾布法、
セラミッック製濾過筒法及び濾過助剤による方法でもよ
いが、精密濾過法によればその濾過液は透明で、魚臭が
なくかつ大腸菌等の存在しない良質な調味液をえること
ができるので好ましい。本発明では調味液廃液に酵素剤
を作用させると同時に、廃液の濃縮も平行して行う。す
なわち本発明では,調味液廃液に酵素剤を添加し、保温
を行いながら減圧蒸留を行うと、廃液中で沸騰現象が生
じるため、十分な撹伴がなされ基質と酵素剤との反応が
促進される。このことから酵素作用と濃縮操作の同時終
了時の廃液が、品質的にバランスがよく、大幅な処理時
間の短縮化を図ることができた。
The seasoning liquid used for aquatic products is prepared by mixing rich soy sauce with additives such as sugar, sugars such as starch syrup and amino acids, so that the sugar content is 45 to 55%. Furthermore, these seasoning liquids, after soaking,
Due to the dehydration effect of the raw material fish, the sugar content is diluted to around 25%, and it has a strong fish odor and becomes a waste liquid with a large amount of eluted protein.
Therefore, for the regeneration of the seasoning liquid waste liquid, it is necessary to decompose and solubilize these eluted components. The use of enzymatic agents is desirable for degrading these proteins in the effluent.
In this case, the waste liquid contains soy sauce as the main component, so the pH is 4.5.
It is in the range of to 5.0. A protease derived from Aspergillus oryzae is suitable as an enzyme agent suitable for decomposing waste liquid in such a low pH range. In the present invention, a commercially available enzyme preparation having a wide range of substrate specificities and having exopeptidase and endopeptidase activities was selected in order to effectively decompose the eluted protein. In addition, regarding the decomposition and removal of lipids that cause fishy odor, since it is partially decomposed by the action of protease, but it is not sufficient, it was solved by filtration using a microfiltration membrane. Here, in the filtration method of the coagulum in the waste liquid, the removal of large ones was carried out by the centrifugal separation method, and the removal of the small ones was carried out by the microfiltration membrane method. In the microfiltration membrane used in the present invention, it was found that the microfiltration membrane can be used to remove fine particles of 0.1 micron or more, and as a result, the fish odor in the waste liquid is effectively eliminated. In addition, a filter cloth method, which is a general filtration method among the filtration methods,
Although the method using a ceramic filter method and a filter aid may be used, the microfiltration method is preferable because the filtrate is transparent and a high-quality seasoning liquid free of fish odor and free of Escherichia coli can be obtained. In the present invention, an enzyme agent is allowed to act on the seasoning liquid waste liquid, and the waste liquid is concentrated in parallel. That is, in the present invention, when an enzyme agent is added to the waste liquid of the seasoning solution and vacuum distillation is performed while maintaining heat, a boiling phenomenon occurs in the waste liquid, so that the reaction between the substrate and the enzyme agent is promoted because sufficient boiling occurs. It From this, the waste liquid at the end of the enzyme action and the concentration operation was well balanced in quality, and the treatment time could be shortened significantly.

【0005】ここで酵素剤の廃液への最小添加量は0.
05%でもよい。これは酵素作用を行わせると同時に、
濃縮を行うため濃縮後では酵素剤の濃度が約1%前後と
なり、酵素反応が十分作用するためである。また廃液が
濃厚である場合は、酵素剤の適正な添加量は0.5%程
度である。これは廃液中に魚類からの塊が相当量溶出し
ているため、酵素作用の対象となる基質の濃度が多量に
存在するためである。また反応温度は40〜60℃の範
囲で十分である。これは温度の設定をボイラーによる蒸
気吹込み式によっているため、温度が変動するためであ
るが、酵素分解作用にはこの範囲で特に問題はない。温
度の保温方法には別にヒータ式等の各種方式があるが、
減圧濃縮を行うため一時的な温度の下降現象がみられる
ことがある。この場合においても保温が40〜60℃の
範囲を保持すれば酵素作用は十分行われる。さらに酵素
作用及び濃縮時間は最小2時間は必要であるが、最大4
8時間でも品質に悪影響は及ぼすことはない。48時間
作用させた場合は反応液の腐敗が懸念されるが、濃縮度
が50%前後の高濃度であるため、微生物の影響はみら
れない。この濃縮は、糖度が30〜60%となるまで行
う。遠心分離の条件は工場現場では、若干遠心分離のた
めの時間を要するものの、少なくとも1分間に5,00
0回転以上は必要である。また実験室レベルでは遠心分
離の条件が、1分間に20,000回転であれば回転時
間は10分間で清澄な▲ろ▼過液をえることができる。
Here, the minimum amount of addition of the enzyme agent to the waste liquid is 0.
It may be 05%. This makes the enzyme work,
This is because the concentration of the enzyme agent becomes about 1% after concentration because the concentration is performed, and the enzyme reaction sufficiently acts. When the waste liquid is thick, the proper amount of the enzyme agent added is about 0.5%. This is because a large amount of lumps from fish have been eluted in the waste liquid, so that there is a large concentration of the substrate that is the target of enzyme action. A reaction temperature of 40 to 60 ° C is sufficient. This is because the temperature fluctuates because the temperature is set by a steam blowing method using a boiler, but there is no particular problem in the enzymatic decomposition action in this range. There are various methods such as a heater method for keeping the temperature,
Since the concentration is performed under reduced pressure, a temporary temperature drop phenomenon may be observed. Even in this case, if the heat retention is maintained in the range of 40 to 60 ° C, the enzyme action is sufficiently performed. Furthermore, the enzyme action and concentration time must be at least 2 hours, but at most 4
Even 8 hours will not adversely affect the quality. When the reaction liquid is left to act for 48 hours, the reaction liquid may be spoiled, but the concentration of the reaction liquid is as high as about 50%, so that the influence of microorganisms is not observed. This concentration is performed until the sugar content reaches 30 to 60%. At the factory, the centrifugation conditions require some time for centrifugation, but at least 5,000 for 1 minute.
0 or more revolutions are required. At the laboratory level, if the centrifugation conditions are 20,000 revolutions per minute, a rotation time of 10 minutes can give a clear filtered liquid.

【0006】[0006]

【実施例】以下実施例について説明するが,本発明はこ
れら実施例にのみ限定されるものではない。 実施例1:調味液の廃液2,000リットルを減圧蒸留
タンク(容量約3m)に投入し、市販酵素剤タシナー
ゼ(協和発酵株式会社製)1kg及びパンチダーゼNP
−2(ヤクルト薬品工業株式会社製)1kgを添加した
後、蒸気を吹き込みながら温度を40〜60℃まで上昇
させることにより、保温(常時蒸気吹き込み)させると
共に、脱気処理(真空度650〜750mmHg)を行
う。保温時間及び脱気処理時間を12〜24時間とす
る。ここで脱気処理を行うことにより、蒸発水量を70
0〜1,000リットルとなるように調整すると同時
に、濃縮液の糖度が30〜60%の酵素反応終了液をえ
る。このものを遠心分離(サイトウ式遠心分離器ADS
1000型:斎藤遠心機工業株式会社製)した後、精密
濾過(株式会社クラレ製、MS−8252タイプ)によ
り膜濾過を行う。漬け込み前の調味液(以下従来液とい
う)、漬け込み後の廃液(以下廃液という)、酵素反応
終了後の濃縮液及び濾過後の調味液(以下本発明液とい
う)の成分分析結果及び粘度試験の結果を表1及び表2
に示す。なお糖度は糖用屈折計の測定値である。表1で
は本発明液の糖度が38.0%に調製した例を示す。
EXAMPLES Examples will be described below, but the present invention is not limited to these examples. Example 1: 2,000 liters of waste liquid of seasoning liquid was put into a vacuum distillation tank (capacity: about 3 m 3 ), 1 kg of commercially available enzyme agent tacinase (manufactured by Kyowa Hakko Co., Ltd.) and Punchdase NP.
-2 (manufactured by Yakult Chemical Industry Co., Ltd.) was added, and then the temperature was raised to 40 to 60 ° C. while blowing steam to keep it warm (constant steam blowing) and degassing (vacuum degree 650 to 750 mmHg). )I do. The heat retention time and the deaeration treatment time are 12 to 24 hours. By performing degassing treatment here, the amount of evaporated water is reduced to 70
The concentration is adjusted to 0 to 1,000 liters, and at the same time, an enzyme reaction completed solution having a sugar content of 30 to 60% is obtained. Centrifuge this (Saito type centrifuge ADS
Model 1000: Saito Centrifuge Industry Co., Ltd.), and then membrane filtration by microfiltration (Kuraray Co., Ltd., MS-8252 type). Component analysis results and viscosity test of seasoning liquid before soaking (hereinafter referred to as conventional liquid), waste liquid after soaking (hereinafter referred to as waste liquid), concentrated liquid after completion of enzymatic reaction and seasoning liquid after filtration (hereinafter referred to as liquid of the present invention) and viscosity test The results are shown in Table 1 and Table 2.
Shown in The sugar content is a value measured by a sugar refractometer. Table 1 shows an example in which the sugar content of the liquid of the present invention was adjusted to 38.0%.

【0007】[0007]

【表1】 [Table 1]

【表2】 [Table 2]

【0008】表2では各種調味液の品質を比較するた
め、糖度を一定(24%)に調製した場合の一般成分値
を示した。企業製造現場における漬け込み方法は、魚
(アナゴ)100kgに対し、調味液10kgを添加
後、温度4℃の冷蔵庫で約16時間保持する方式であ
る。その結果表1に示すように、従来液で糖度61.4
%であった濃厚な調味液が、漬け込み後の廃液では糖度
24.0%に希釈される。ここで漬け込み後の糖度の希
釈度について、漬け込む魚類、魚体の大きさ及漬け込み
時間によって異なるが、概略20〜40%の範囲にあ
る。この希釈の原因は漬け込み工程中に、調味液中の成
分が魚肉へ浸透すると同時に、魚肉中の水分が調味液中
へ溶出されることによるためである。 このため調味液
は希釈されると同時に腐敗し易くなる。従って漬け込み
後のこれらの廃液は、魚肉中からの蛋白質が増加してい
るため、表2に示すように粘度が高くなるので,再度漬
け込み液として利用できないという欠点がある。そこで
廃液へ酵素剤を添加作用させることにより、魚肉からの
溶出成分を分解しかつ可溶化する。酵素反応処理後の廃
液の粘度は、表2に示すごとく、廃液と比較して小さく
なっていることが分かる。
In order to compare the qualities of various seasoning liquids, Table 2 shows general component values when the sugar content is adjusted to be constant (24%). The soaking method at a company manufacturing site is a method of adding 10 kg of seasoning liquid to 100 kg of fish (egg) and holding it in a refrigerator at a temperature of 4 ° C. for about 16 hours. As a result, as shown in Table 1, the sugar content of the conventional liquid was 61.4.
The concentrated seasoning liquid, which had a concentration of%, is diluted to a sugar content of 24.0% in the waste liquid after pickling. The degree of dilution of the sugar content after soaking depends on the fish to be soaked, the size of the fish body and the soaking time, but is generally in the range of 20 to 40%. The cause of this dilution is that the components in the seasoning liquid permeate into the fish meat during the pickling process and, at the same time, the water in the fish meat is eluted into the seasoning liquid. For this reason, the seasoning liquid is diluted and at the same time easily decomposed. Therefore, these waste liquids after pickling have a drawback that they cannot be used as pickling liquids again because the proteins from fish meat are increased and the viscosity becomes high as shown in Table 2. Therefore, by adding an enzyme agent to the waste liquid, the components eluted from fish meat are decomposed and solubilized. As shown in Table 2, it can be seen that the viscosity of the waste liquid after the enzymatic reaction treatment is smaller than that of the waste liquid.

【0009】また味における旨味の指標について、酸度
1に関与する成分は有機酸、酸性アミノ酸であり、酸度
2は中性及び塩基性アミノ酸が主要ものである。表2に
示すように調味液は漬け込みことにより、酸度 1及び
酸度2が増加していることから、呈味成分であるアミノ
酸等が増加している。すなわちエキスが溶出し呈味成分
は向上していることから、調味液として再生する価値は
十分にあることがわかる。ここで本発明に係る再生調味
液の製造方法として実施例1では、遠心分離後濾過する
方式を採用しているが、廃液の性質によっては遠心分離
を行った後の分離液のみで再度、漬け込み液として利用
できる。なお魚臭の原因となる脂質の除去の効果は、表
2に示すように酵素処理によりわずかに減少するもの
の、その効果は期待できる程大きなものではない。しか
し酵素反応終了後の濃縮液を精密濾過膜処理することに
より、魚臭の除去が可能となる。このことは本発明再生
調味液を再度魚に添加した場合、香りについては特に問
題がないことを示すものである。本発明液のメリット
は、色調が従来液よりも淡くなるということであり、こ
のことは漬け込み後の魚の色調を向上させる効果をもつ
ものである。すなわち本発明液は、従来液と比較して
呈味成分の増加及び色調の向上のメリットをえることが
できる。そこで本発明液と従来液との漬け込み効果の比
較を更に以下の実施例2及び実施例3の試験にしたがっ
て検討した。
Regarding the umami taste index, the components involved in acidity 1 are organic acids and acidic amino acids, and acidity 2 is mainly neutral and basic amino acids. As shown in Table 2, when the seasoning liquid is soaked, the acidity 1 and the acidity 2 are increased, and thus the amino acids and the like which are taste components are increased. That is, since the extract is eluted and the taste component is improved, it can be seen that it has a sufficient value to be regenerated as a seasoning liquid. Here, as a method for producing the regenerated seasoning liquid according to the present invention, in Example 1, a method of centrifuging and then filtering is adopted. However, depending on the nature of the waste liquid, only the separated liquid after centrifugation is used to soak again. It can be used as a liquid. The effect of removing lipids that cause fishy odor is slightly reduced by the enzyme treatment as shown in Table 2, but the effect is not as large as expected. However, the fish odor can be removed by subjecting the concentrated liquid after the enzymatic reaction to microfiltration membrane treatment. This shows that when the regenerated seasoning liquid of the present invention is added to fish again, there is no particular problem regarding the scent. The advantage of the liquid of the present invention is that the color tone becomes lighter than that of the conventional liquid, which has the effect of improving the color tone of the fish after pickling. That is, the liquid of the present invention is
It is possible to obtain the merits of increasing taste components and improving color tone. Therefore, a comparison of the soaking effect between the liquid of the present invention and the conventional liquid was further examined according to the tests of Examples 2 and 3 below.

【0010】実施例2:白身の魚に対する本発明液の漬
け込み効果を調べるために、アナゴの切身(肉厚4mm
×幅35〜40mm×長さ150mm)125gを30
0ml容ビーカ−へ、従来液及び本発明液をそれぞれ1
25g添加した後、4℃の冷蔵庫内にて16時間漬け込
む。その後アナゴをホモジナイズした後、その濾過液の
分析を行った。
Example 2: In order to investigate the pickling effect of the liquid of the present invention on white fish, eel fillets (thickness: 4 mm)
X width 35-40 mm x length 150 mm) 125 g 30
Add 1 part each of the conventional solution and the solution of the present invention to a 0 ml beaker.
After adding 25 g, soak in a refrigerator at 4 ° C. for 16 hours. After that, the eel was homogenized, and then the filtrate was analyzed.

【0011】[0011]

【表3】 [Table 3]

【0012】表3の結果から、従来液及び本発明液とも
糖度、食塩濃度等に及ぼす影響について実質的に差はみ
られないが、発明液のアナゴの色調の淡色化の効果が認
められた。
From the results shown in Table 3, there is substantially no difference between the conventional solution and the solution of the present invention in terms of sugar content, salt concentration, etc., but the effect of lightening the color tone of the eel of the invention solution was recognized. .

【0013】実施例3:赤身の魚に対する本発明液の漬
け込み効果を調べるために、小アジの切身(肉厚20〜
30mm×幅35〜40mm×長さ20mm)100g
を300ml容ビーカ−へ、従来液及び本発明液をそれ
ぞれ100g添加した後、4℃の冷蔵庫内にて16時間
漬け込む。その後小アジをホモジナイズした後、その濾
過液の分析を行った。その結果を表4に示す。
Example 3: To examine the pickling effect of the liquid of the present invention on red fish, small horse mackerel fillets (thickness 20-
30mm x width 35-40mm x length 20mm) 100g
100 g of each of the conventional solution and the solution of the present invention were added to a 300 ml beaker and then immersed in a refrigerator at 4 ° C. for 16 hours. After that, after homogenizing the small horse mackerel, the filtrate was analyzed. The results are shown in Table 4.

【0014】[0014]

【表4】 [Table 4]

【0015】表4にみられるごとく,アナゴにおける結
果と同様に、糖度及び食塩濃度については、従来液と本
発明液とは実質的に差はみられないが、色調において淡
色化の効果が認められた。以上の結果より、本発明液は
従来液と比較して、成分的には実質的に同等であるが、
むしろ色調において良好な成果をえることができた。す
なわち従来では廃液として廃棄されていたものの有効利
用技術を確立することができた。
As shown in Table 4, similar to the results in Anago, there is no substantial difference in sugar content and salt concentration between the conventional solution and the solution of the present invention, but the effect of lightening the color tone is recognized. Was given. From the above results, the liquid of the present invention is substantially equivalent in composition as compared with the conventional liquid,
Rather, we were able to obtain good results in color tone. That is, it was possible to establish an effective utilization technology of what was conventionally discarded as a waste liquid.

【0016】[0016]

【発明の効果】以上のごとく本発明方法では,水産物を
調味液に浸漬して味付けする漬け込み工程後に生じる糖
度が20〜40%の調味液廃液へ,麹菌由来のプロテア
ーゼを0.05〜0.5%となるように添加し,酵素反
応温度40〜60℃,反応時間2〜48時間で酵素反応
を行わせながら糖度30〜60%まで減圧濃縮後,▲ろ
▼過又は遠心分離後▲ろ▼過して再生調味液を取得する
もので、調味液廃液に酵素反応と減圧蒸留濃縮の同時平
行処理を行うため、廃液中で沸騰現象が生じて、十分な
撹伴がなされ基質と酵素剤との反応が大いに促進され
る。またその結果、酵素作用と濃縮操作の同時終了時の
廃液が、品質的にバランスがよいものとなり、そして大
幅な処理時間の短縮化を図ることができる。また、減圧
蒸留濃縮後に、遠心分離による懸濁物の処理及び▲ろ▼
過を行えば,調味液廃液から新製品に比べてと何ら遜色
のない再生調味液を製造できると共に,更に漬け込み用
魚類の色調を向上させるという顕著な効果を奏する。以
上本発明方法により,従来では廃液として廃棄処分され
ていた調味液廃液の有効利用のリサイクル化技術が十分
に確立できる。
INDUSTRIAL APPLICABILITY As described above, according to the method of the present invention, the protease derived from Aspergillus oryzae is added to the waste liquid of the seasoning liquid having a sugar content of 20 to 40% after the soaking process in which the marine product is dipped in the seasoning liquid and seasoned. It is added to 5%, and the enzyme reaction is carried out at an enzyme reaction temperature of 40 to 60 ° C. and a reaction time of 2 to 48 hours, and then concentrated under reduced pressure to a sugar content of 30 to 60%, after filtration or after centrifugation. ▼ To obtain regenerated seasoning liquid, the seasoning liquid waste liquid is subjected to simultaneous parallel processing of enzymatic reaction and vacuum distillation concentration, so boiling phenomenon occurs in the waste liquid, and the substrate and enzyme agent are sufficiently stirred. The reaction with is greatly promoted. Further, as a result, the waste liquid at the end of simultaneous enzyme action and concentration operation has a good quality balance, and the processing time can be greatly shortened. After concentration under reduced pressure, the suspension is treated by centrifugation and filtered.
By doing so, a regenerated seasoning liquid that is no better than the new product can be produced from the waste liquid of the seasoning liquid, and the remarkable effect of further improving the color tone of the fish for pickling is exhibited. As described above, according to the method of the present invention, a recycling technique for effectively utilizing the seasoning liquid waste liquid, which has been conventionally discarded as a waste liquid, can be sufficiently established.

フロントページの続き (56)参考文献 特開 昭63−91046(JP,A) 特開 平1−187065(JP,A) 特開 平4−197151(JP,A)Continuation of the front page (56) Reference JP-A 63-91046 (JP, A) JP-A 1-187065 (JP, A) JP-A 4-197151 (JP, A)

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 水産物を調味液に浸漬して味付けする漬
け込み工程後に生じる糖度が20〜40%の調味液廃液
へ,麹菌由来のプロテアーゼを0.05〜0.5%とな
るように添加し,酵素反応温度40〜60℃,反応時間
2〜48時間で酵素反応を行わせながら糖度30〜60
%まで減圧蒸留濃縮後,▲ろ▼過又は遠心分離後▲ろ▼
過して再生調味液を取得することを特徴とする調味液廃
液の再生処理方法。
1. A koji mold-derived protease is added to a waste liquid of a seasoning liquid having a sugar content of 20 to 40%, which is produced after the soaking step of dipping a marine product in a seasoning liquid so as to be 0.05 to 0.5%. , Enzymatic reaction temperature 40 to 60 ° C, reaction time 2 to 48 hours, while performing enzymatic reaction, sugar content 30 to 60
% After vacuum distillation and concentration, and after filtration or centrifugation.
A method for reclaiming a waste seasoning liquid, which comprises recovering the seasoning liquid after passing through.
【請求項2】 遠心分離の回転数が,5,000〜2
0,000回転/分であることを特徴とする請求項1記
載の調味液廃液の再生処理方法。
2. The number of revolutions of centrifugation is 5,000 to 2.
The method for regenerating a seasoning liquid waste according to claim 1, wherein the number of revolutions is 10,000 rpm.
【請求項3】 ▲ろ▼過が,精密▲ろ▼過であることを
特徴とする請求項1記載の調味液廃液の再生処理方法。
3. The method for regenerating a seasoning liquid waste liquid according to claim 1, wherein the filtration is a precision filtration.
JP5187401A 1993-06-30 1993-06-30 Reprocessing method of seasoning liquid waste Expired - Fee Related JP2545330B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5187401A JP2545330B2 (en) 1993-06-30 1993-06-30 Reprocessing method of seasoning liquid waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5187401A JP2545330B2 (en) 1993-06-30 1993-06-30 Reprocessing method of seasoning liquid waste

Publications (2)

Publication Number Publication Date
JPH0716073A JPH0716073A (en) 1995-01-20
JP2545330B2 true JP2545330B2 (en) 1996-10-16

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Country Link
JP (1) JP2545330B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101283680B1 (en) * 2010-07-20 2013-07-08 김형수 Method for preparing salted anchovy sauce, and method for preparing soybean paste and soy sauce using thereof
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6391046A (en) * 1986-10-06 1988-04-21 Kikkoman Corp Heat-treatment of liquid containing thermally coagulable protein
JPH0657122B2 (en) * 1988-01-20 1994-08-03 株式会社ハチテイ Method for producing natural seasoning using effluent during food processing
JPH04197151A (en) * 1990-11-28 1992-07-16 Hachitei:Kk Production of natural seasoning

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