JP3268657B2 - How to remove heavy metals from amino acid solution of fish and shellfish - Google Patents
How to remove heavy metals from amino acid solution of fish and shellfishInfo
- Publication number
- JP3268657B2 JP3268657B2 JP24043792A JP24043792A JP3268657B2 JP 3268657 B2 JP3268657 B2 JP 3268657B2 JP 24043792 A JP24043792 A JP 24043792A JP 24043792 A JP24043792 A JP 24043792A JP 3268657 B2 JP3268657 B2 JP 3268657B2
- Authority
- JP
- Japan
- Prior art keywords
- fish
- shellfish
- amino acid
- acid solution
- heavy metals
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
Landscapes
- General Preparation And Processing Of Foods (AREA)
- Soy Sauces And Products Related Thereto (AREA)
- Meat, Egg Or Seafood Products (AREA)
- Processing Of Solid Wastes (AREA)
- Treatment Of Liquids With Adsorbents In General (AREA)
- Fertilizers (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、魚貝類アミノ酸液から
重金属類を除去する方法に関し、より詳細には、魚貝類
の加工残滓の一つであるホタテ貝の中腸線などから有害
物質とされるカドミウムなど重金属類を除去し、有害金
属を含む魚貝類を資源としての利用拡大と公害源の抑制
を可能とする魚貝類アミノ酸液から重金属類を除去する
方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for removing heavy metals from an amino acid solution of fish and shellfish, and more particularly to a method for removing harmful substances from the mid-gut line of scallops, which is one of the processing residues of fish and shellfish. The present invention relates to a method for removing heavy metals from fish and shellfish amino acid liquids, which removes heavy metals such as cadmium, and makes it possible to expand the use of fish and shellfish containing harmful metals as resources and to reduce pollution sources.
【0002】[0002]
【従来の技術】従来、魚貝類の加工残滓を有効利用した
水産食品としては、缶詰、煮干し、煮熟製品及び魚粕ミ
ールなどを製造する際に副生する煮汁、蒸煮ドリップを
濃縮したもの、この濃縮物を酵素剤で消化させたもの、
魚貝類を加工する際に副生する頭・皮・骨・内臓などの
不可食部を有機、無機酸又は酵素剤で消化させたもの、
及び魚貝類の肉や内臓に塩を用い長期に亘り自己消化さ
せた旨味調味料などが挙げられる。2. Description of the Related Art Conventionally, seafood products that effectively utilize processed residues of fish and shellfish include concentrated soups and steamed drip by-products when producing canned, dried and boiled products and fish cake meal. , This concentrate is digested with an enzyme preparation,
Inedible parts such as the head, skin, bones, and internal organs that are by-produced when processing fish and shellfish are digested with organic, inorganic acids, or enzyme agents.
And umami seasonings which have been self-digested over a long period of time using salt for meat and internal organs of fish and shellfish.
【0003】ところで、魚貝類は食物連鎖に起因すると
される重金属類が多少に拘らず蓄積され、特に内臓類の
内、肝臓、腎臓又はこれらの機能に相当する臓器類に多
く蓄積されている。殊にホタテ貝の中腸腺には高濃度の
カドミウムなどの重金属が蓄積されているため、資源と
して利用されることなく、土中埋没あるいは焼却処分さ
れている。[0003] By the way, in fish and shellfish, heavy metals attributed to the food chain are accumulated to some extent, and particularly, among the internal organs, a large amount is accumulated in the liver, kidney or organs corresponding to these functions. In particular, heavy metals such as cadmium are accumulated in the midgut glands of scallop, and are buried in soil or incinerated without being used as resources.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、カドミ
ウムなどの重金属が高濃度に蓄積されているホタテ貝の
中腸腺や魚介類の内臓などを土中埋没による処分方法
は、埋立処分地からの悪臭やハエの発生やカラスの餌場
となるなどの公害源となったり、浸出する腐敗汁による
河川などの汚染や周囲の草木を枯死を招き、更には埋立
地の確保が困難となっている。However, the disposal method of scallop midgut glands and fish and shellfish containing cadmium and other heavy metals at high concentration by burial in the soil is not suitable for odor from landfill sites. It becomes a source of pollution, such as the occurrence of flies and flies, and a source of crows. It also pollutes rivers and other vegetation due to decayed decay juice, and makes it difficult to secure landfill sites.
【0005】この埋立地の確保の困難性に鑑み、焼却処
分するよう工夫がなされているが、この処分方法は、6
00〜800°Cで焼却するもので、カドミウムの融
点、沸点以上に加熱すると空中飛散する恐れがあり、し
かもタンパクの焼け焦げによる特有の悪臭を発生させる
など、新たな公害源としての問題を呈している。[0005] In view of the difficulty in securing this landfill, various measures have been taken to incinerate it.
It is incinerated at 00 to 800 ° C. If heated above the melting point and the boiling point of cadmium, it may be scattered in the air, and it presents a problem as a new pollution source, such as generating a peculiar odor due to burning of the protein. I have.
【0006】本発明は、このような実情に鑑み創案され
たものであって、魚貝類のタンパク質に蓄積されている
カドミウムなどの重金属を生成されるアミノ酸液に移行
させ、このアミノ酸液に溶存するカドミウムなどの重金
属を除去する方法を提供することを目的とする。The present invention has been made in view of such circumstances, and transfers heavy metals such as cadmium accumulated in proteins of fish and shellfish to a produced amino acid solution and dissolves in the amino acid solution. It is an object to provide a method for removing heavy metals such as cadmium.
【0007】[0007]
【課題を解決するための手段】本発明者らは、上記課題
を解決すべく鋭意研究した結果、魚貝類のタンパク質に
結合する重金属を酸類に溶解させ、この溶解した重金属
を酸類による加水分解により生成されるアミノ酸液に移
行させ、所定の条件下でのみ選択的にこのアミノ酸に溶
存する重金属を分離、除去することに成功し、単に公害
の発生源を抑制できるに止まらず、資源として利用拡大
しうることをも見出し、本発明に係る魚貝類のアミノ酸
液から重金属類を除去する方法を完成した。Means for Solving the Problems The present inventors have made intensive studies to solve the above-mentioned problems, and as a result, dissolved heavy metals binding to proteins of fish and shellfish in acids, and hydrolyzed the dissolved heavy metals by acids. Transfer to the generated amino acid solution, succeeded in selectively separating and removing heavy metals dissolved in this amino acid only under predetermined conditions, and not only can reduce the source of pollution, but also expand its use as a resource The present inventors have also found that the method for removing heavy metals from the amino acid solution of fish and shellfish according to the present invention has been completed.
【0008】即ち、本発明に係る魚貝類のアミノ酸液か
ら重金属類を除去する方法は、pHを8〜9に調製した
魚貝類アミノ酸液にキレート剤を添加し作用させ、該キ
レート剤に前記魚貝類アミノ酸液に含まれる重金属類を
吸着させることを、その解決手段としている。That is, in the method for removing heavy metals from the amino acid solution of fish and shellfish according to the present invention, a chelating agent is added to the amino acid solution of fish and shellfish whose pH is adjusted to 8 to 9 to cause the chelating agent to act. The solution is to adsorb heavy metals contained in the shellfish amino acid solution.
【0009】また、本発明に係る魚貝類アミノ酸液から
重金属類を除去する方法は、pHを4以下で20〜50
°Cの温度に調製された醗酵槽で魚貝類タンパク質を自
己消化により及び必要に応じてプロテアーゼを作用させ
て前記魚貝類タンパク質をアミノ酸液まで分解し、次い
でpHを8〜9に調製された魚貝類アミノ酸液にキレー
ト剤を添加し作用させ、該キレート剤に前記魚貝類アミ
ノ酸液に含まれる重金属類を吸着させるこを、その解決
手段としている。The method for removing heavy metals from the amino acid solution of fish and shellfish according to the present invention is characterized in that the pH is 4 or less and the pH is 20 to 50.
The fish and shellfish protein is decomposed into an amino acid solution by self-digestion of the fish and shellfish protein in a fermenter adjusted to a temperature of ° C. and, if necessary, by the action of a protease, and then the fish is adjusted to pH 8 to 9. The solution is to add a chelating agent to the shellfish amino acid solution to cause the chelating agent to adsorb heavy metals contained in the fish and shellfish amino acid solution.
【0010】更に、本発明に係る魚貝類アミノ酸液から
重金属類を除去する方法は、細砕した魚貝類のpHが4
以下になる条件で酸類を作用させて前記魚貝類タンパク
質を加水分解し、次いで20〜50°Cの温度に調製さ
れた醗酵槽で魚貝類タンパク質を自己消化により及び必
要に応じてプロテアーゼを作用させて前記魚貝類タンパ
ク質をアミノ酸液まで分解し、更にpHを8〜9に調製
された魚貝類アミノ酸液にキレート剤を添加し作用さ
せ、該キレート剤に前記魚貝類アミノ酸液に含まれる重
金属類を吸着させるこを、その解決手段としている。Further, the method for removing heavy metals from the amino acid solution of fish and shellfish according to the present invention is characterized in that the pH of the crushed fish and shellfish is 4 or less.
The fish and shellfish protein is hydrolyzed by the action of acids under the following conditions, and then the fish and shellfish protein is autolyzed in a fermenter prepared at a temperature of 20 to 50 ° C., and the protease is allowed to act as necessary. To decompose the fish and shellfish protein into an amino acid solution, and further add a chelating agent to the fish and shellfish amino acid solution adjusted to pH 8 to 9 to cause the chelating agent to remove heavy metals contained in the fish and shellfish amino acid solution. Adsorption is the solution.
【0011】以下、本発明に係る魚貝類アミノ酸液から
重金属類を除去する方法について更に詳細に説明する。Hereinafter, the method for removing heavy metals from the amino acid solution of fish and shellfish according to the present invention will be described in more detail.
【0012】本発明は、特にその理論にこだわる訳では
ないが、魚貝類タンパク質に結合しているカドミウムが
酸類に溶解する性質に着目し、まずこの溶解されたカド
ミウムを酸類により生成されたアミノ酸液に移行させ、
次いでpHを8〜9に調製された魚貝類アミノ酸液にキ
レート剤を添加し作用させ、該キレート剤に前記魚貝類
アミノ酸液に含まれる重金属類を吸着させ、重金属類を
選択的に分離、抽出除去できることをはじめて見出した
ことに基づく。Although the present invention is not particularly limited to the theory, the present invention pays attention to the property that cadmium bound to fish and shellfish proteins dissolves in acids, and firstly, dissolves the dissolved cadmium into an amino acid solution produced by acids. To
Next, a chelating agent is added to the fish and shellfish amino acid solution adjusted to pH 8 to 9 to act thereon, and the chelating agent is allowed to adsorb heavy metals contained in the fish and shellfish amino acid solution to selectively separate and extract heavy metals. Based on first finding that it can be removed.
【0013】ところで、カドミウムは金属と硫黄を含ん
だ分子量凡そ6000のメタロチオネインと呼ばれるタ
ンパクと結合していることが知られ、また酸性に溶解
し、アルカリ性側では水酸化カドミウムとなり沈澱す
る。By the way, cadmium is known to be bound to a protein called metallothionein containing a metal and sulfur and having a molecular weight of about 6000, and is dissolved acidicly and precipitates as cadmium hydroxide on the alkaline side.
【0014】本発明では、このようなカドミウムの性質
を利用して、まずミートチョッパーなどで細砕した原料
となる魚貝類を無機もしくは有機の酸類、例えば塩酸、
酢酸でpHを4以下に調製し、魚貝類タンパク質をアミ
ノ酸液まで加水分解する。ここでpHを「4以下」とし
たのは酸類の作用により、カドミウムを溶解させ遊離さ
せること、及び魚貝類タンパク質の加水分解、醗酵作用
における腐敗に関与する細菌群の活動を抑制できるから
である。これにより魚貝類タンパク質に結合したカドミ
ウムなどの重金属がアミノ酸液に移行し、溶存状態で存
在させることができる。In the present invention, utilizing such properties of cadmium, first, fish or shellfish, which is a raw material crushed by a meat chopper or the like, is converted into an inorganic or organic acid such as hydrochloric acid.
The pH is adjusted to 4 or less with acetic acid, and the fish and shellfish proteins are hydrolyzed to an amino acid solution. Here, the pH is set to “4 or less” because the action of acids can dissolve and release cadmium, and can inhibit the activity of bacteria involved in spoilage in the hydrolysis and fermentation of fish and shellfish proteins. . As a result, heavy metals such as cadmium bound to the fish and shellfish proteins migrate to the amino acid solution and can be present in a dissolved state.
【0015】この状態は、酸類に加えて原料に含まれる
自己消化酵素の作用及び必要に応じてプロテアーゼを作
用させること、及び攪拌による機械的剪断を与えること
で、より効果的に達成することができる。 即ち原料に
酸類を作用させpH値を4以下とし20〜50°Cの温
度に調製された醗酵槽で自己消化酵素の働きと攪拌によ
る機械的剪断により、加水分解がより効果的に進行し、
必要に応じてプロテアーゼを作用させることで更に効果
的に進行する。ここで温度を「20〜50°C」に限定
したのは、この範囲内で酵素が最も効果的に作用するか
らである。This condition can be more effectively achieved by the action of the autolyzing enzyme contained in the raw material in addition to the acids and the action of the protease if necessary, and the application of mechanical shearing by stirring. it can. That is, the action of the acids on the raw material to adjust the pH value to 4 or less and the hydrolysis of the fermenter prepared at a temperature of 20 to 50 ° C. by the action of the autolyzing enzyme and the mechanical shearing by stirring more effectively proceed,
The reaction proceeds more effectively by acting a protease as necessary. The reason why the temperature was limited to “20 to 50 ° C.” is that the enzyme works most effectively within this range.
【0016】こうして得られるアミノ酸液は、粘稠性の
ある懸濁した液化物となっているため、固液分離及び油
脂分離により、それぞれ固形分及び油脂分を除去し、精
製する。これらの工程はキレート剤を作用させる前処理
工程として望ましい。Since the amino acid solution thus obtained is a viscous suspended liquefied product, the solid content and the fat content are removed and purified by solid-liquid separation and oil / fat separation, respectively. These steps are desirable as a pretreatment step for allowing the chelating agent to act.
【0017】精製されたアミノ酸液に苛性ソーダ、アン
モニアなどでpH8〜9に調製した後、キレート剤、例
えばメチルイソブチルケトン(以下、MIBKと言う)
と、これに対応する溶剤として、例えばジエチルジチオ
カルバミン酸(以下、DDTCと言う)とを作用させ
て、カドミウムを吸着させる。この作用を有するキレー
ト剤は他にも幾つか挙げられ、実施例に例示したものに
限定されないことは言うまでもない。After the purified amino acid solution is adjusted to pH 8 to 9 with caustic soda, ammonia or the like, a chelating agent such as methyl isobutyl ketone (hereinafter referred to as MIBK)
Cadmium is adsorbed by reacting, for example, diethyldithiocarbamic acid (hereinafter referred to as DDTC) as a solvent corresponding thereto. There are several other chelating agents having this effect, and it goes without saying that the chelating agents are not limited to those exemplified in the examples.
【0018】溶剤、溶媒、溶質の混合、合一は、攪拌
型、遠心力型、振動型が用いられるが、中でも渦流攪拌
型が最も効果的である。この混合、合一された混合液を
塔型などの分離槽により、溶媒、溶剤と溶質とに分離さ
せ、溶剤、溶媒を抽出し、次いでこの分離液を減圧など
により濃縮して製品とする。A stirring type, a centrifugal type and a vibration type are used for mixing and coalescing of a solvent, a solvent and a solute, and among them, a vortex type is most effective. The mixed and unified liquid mixture is separated into a solvent, a solvent and a solute by a separation tank such as a tower, and the solvent and the solvent are extracted. Then, the separated liquid is concentrated under reduced pressure or the like to obtain a product.
【0019】なお、本発明を実施する際に特に重視しな
ければならないのは処理工程における嫌気性の醗酵、分
解である。通常生鮮ホタテ貝の貝柱を除いた中腸腺を含
む内臓塊には、多くの砂や貝片が抱かれおり、醗酵処理
工程において沈降し、堆積するためデットスペースとな
り、この部分が嫌気性の醗酵となる。嫌気性醗酵は製品
を粗悪なものとし、場合によっては仕掛品全部を投棄し
なければならない。貝片の多くは原料の肉に刺り込んで
おり、一次洗浄、二次洗浄により予めこの貝片を除去す
るのが望ましい。一次洗浄、二次洗浄用に供する装置は
ホタテ貝内臓処理のため特別に用意されたものである。In carrying out the present invention, anaerobic fermentation and decomposition in the treatment step must be particularly emphasized. The visceral mass, including the midgut gland, excluding the scallop of the fresh scallop, usually contains a lot of sand and shell pieces, which sediment and deposit in the fermentation process, forming a dead space. It becomes fermentation. Anaerobic fermentation degrades the product and, in some cases, has to dump the entire work in process. Most of the shell pieces are stabbed in the raw meat, and it is desirable to remove the shell pieces in advance by primary washing and secondary washing. The equipment used for the primary washing and the secondary washing is specially prepared for the treatment of the internal organs of scallops.
【0020】以上の工程を経て得られる濃縮して製品
は、カドミウムなどの重金属の含有量が安全性を確保す
るための規制基準値より大幅に低下されるため、単に公
害の発生源を抑制できるに止まらず、農作物などの肥料
などの資源として利用できる。In the concentrated product obtained through the above-mentioned steps, the content of heavy metals such as cadmium is greatly reduced from the regulation standard value for ensuring safety, so that the source of pollution can be simply suppressed. It can be used as a resource for fertilizers such as agricultural products.
【0021】[0021]
【実施例】以下、本発明に係る魚貝類のアミノ酸液から
重金属類を除去する方法の詳細な説明を実施例に基づい
て説明するが、これらの実施例に限定されるものではな
い。EXAMPLES Hereinafter, the method for removing heavy metals from the amino acid solution of fish and shellfish according to the present invention will be described in detail with reference to examples, but the present invention is not limited to these examples.
【0022】実施例 1 魚貝類のアミノ酸液からの重
金属類の除去法 以下、魚貝類のアミノ酸液から重金属類を除去する方法
について、各工程毎に説明する。 Example 1 Weight of fish and shellfish from amino acid solution
The following method for removing metals, the method for removing heavy metals from acid solutions of fish and shellfish, the respective steps will be described.
【0023】(1)第1工程(第一洗浄) 原料であるホタテ貝の貝柱を除いた後、特別に用意され
たストレーナー構造型の回転篩を内蔵させた改良型魚洗
機により約40〜45°Cの温水を用いて3〜4分間通
過させて原料に含まれる砂、貝片や附着する汚物を除去
した。この工程により、ホタテ貝の中腸腺を含む内臓塊
から概ね砂、貝片を除去できる。 (1) First Step (First Washing) After removing the scallops of the scallop, which is a raw material, about 40 to 40-minutes are obtained by an improved fish washer incorporating a specially prepared rotating sieve of a strainer structure type. Sand was passed through the raw material at 45 ° C. for 3 to 4 minutes to remove sand, shell pieces and attached dirt. By this step, sand and shell pieces can be removed from the visceral mass including the midgut gland of the scallop.
【0024】(2)第2工程(第二洗浄) 上記第一洗浄で除去しきれない砂、貝片を特別に用意さ
れたストレーナー構造型の無限軌道のコンペアを内蔵さ
せた改良型煮熟釜により約40〜45°Cの温湯中を湯
洗いしながら、約10分間通過させて除去した。この
砂、貝片の除去に際しては、原料を載せたコンペアーの
裏側から圧搾空気により温湯中を原料が踊るように操作
しつつ砂、貝片を除去した。この工程により、砂、貝片
が除去され、品温が40°C以上の洗浄されたホタテ貝
の内臓塊が得られる。 (2) Second Step (Second Washing) An improved cooker with a built-in strainer-structured endless track specially prepared for sand and shell pieces that cannot be completely removed by the first washing. While passing through hot water of about 40 to 45 ° C. for about 10 minutes while washing with hot water. In removing the sand and shell pieces, the sand and shell pieces were removed from the back side of the compare on which the raw materials were placed while operating the raw materials in hot water with compressed air so as to dance. By this step, sand and shell pieces are removed, and a visceral mass of scallops washed at a temperature of 40 ° C. or higher is obtained.
【0025】(3)第3工程(細砕) 上記洗浄工程で洗浄された原料をミートチョッパーで細
砕した。 (3) Third Step (Crushing) The raw material washed in the washing step was crushed by a meat chopper.
【0026】(4)第4工程(pH調製) ミートチョッパーで細砕した原料を耐強酸性の容器に収
容し、塩酸を添加してpHが4〜3.8程度になるよう
に調製した。 (4) Fourth Step (Preparation of pH) The raw material crushed by the meat chopper was placed in a strong acid-resistant container, and hydrochloric acid was added to adjust the pH to about 4 to 3.8.
【0027】(5)第5工程(醗酵) pH調製した原料を恒温醗酵槽に収容した後、45°C
で14時間以上連続攪拌し、醗酵消化させた。 (5) Fifth Step (Fermentation) After the pH-adjusted raw material is stored in a constant temperature fermentation tank,
For 14 hours or more to ferment and digest.
【0028】(6)第6工程(固液分離) 醗酵消化物を85〜90°Cに加熱し、スクリュー式デ
カンターにより固形物を分離して分離液を得た。固液分
離による残渣のカドミウム検出量は0.8ppmであっ
た。 (6) Sixth Step (Solid-Liquid Separation) The fermentation digest was heated to 85 to 90 ° C., and the solid was separated by a screw type decanter to obtain a separated liquid. The amount of cadmium detected in the residue by solid-liquid separation was 0.8 ppm.
【0029】(7)第7工程(油脂分離) 固液分離により分離した分離液に懸濁する油脂をディス
ク式デカンターにより分離した。油脂分離後の分離液中
のカドミウム検出量は14ppmであった。 (7) Seventh Step (Oil Separation) Oils and fats suspended in the separated liquid separated by solid-liquid separation were separated by a disk type decanter. The amount of cadmium detected in the separated solution after the separation of the oil and fat was 14 ppm.
【0030】(8)第8工程(pH調製) 油脂分離後の分離液を苛性ソーダを用いてpH8〜9に
調製した。分離液のpHを酸性領域からアルカリ性領域
に移行させることにより、カドミウムとキレート剤との
反応が容易となる。 (8) Eighth Step (pH Adjustment) The separated liquid after the separation of the oil and fat was adjusted to pH 8 to 9 using caustic soda. By shifting the pH of the separated solution from the acidic region to the alkaline region, the reaction between cadmium and the chelating agent becomes easy.
【0031】(9)第9工程(抽出) pHをアルカリ性領域にした調製液にキレート剤として
MIBKと、これに対応する溶媒としてDDTCを添加
して渦流攪拌槽を用いて抽出した。この方法によれば、
攪拌槽に備えつけた攪拌翼に渦流を起こさせる構造であ
るため、溶剤、溶媒、溶質を均一に早く混合できる。こ
の槽は雑菌の侵入、予防のため40°C以上の保温が必
要である。約15〜20分攪拌混合させた後、分離槽に
移送した。 (9) Ninth Step (Extraction) MIBK as a chelating agent and DDTC as a corresponding solvent were added to the prepared solution in which the pH was adjusted to an alkaline region, and the mixture was extracted using a vortex stirring tank. According to this method,
Since the structure is such that a vortex is generated in the stirring blade provided in the stirring tank, the solvent, the solvent, and the solute can be uniformly and quickly mixed. This tank needs to be kept at a temperature of 40 ° C. or more to prevent invasion and prevention of various bacteria. After stirring and mixing for about 15 to 20 minutes, the mixture was transferred to a separation tank.
【0032】(10)第10工程(分離) 搭型の分離槽により浮上する溶媒、溶剤を吸引分離し
た。抽出分離した後の分離液中のカドミウム検出量は
0.15ppmであった。この結果は、肥料などの安全
性を確保するための規制基準を大幅に下回るものであ
る。 (10) Tenth Step (Separation) The solvent floating in the separation tank mounted on the tank and the solvent were separated by suction. The amount of cadmium detected in the separated solution after the extraction and separation was 0.15 ppm. This result is far below the regulatory standards for ensuring the safety of fertilizers.
【0033】(11)第11工程(濃縮) 分離液を減圧加熱濃縮により濃縮し、製品とした。 (11) Eleventh Step (Concentration) The separated liquid was concentrated by heating under reduced pressure to obtain a product.
【0034】実施例 2 魚貝類のアミノ酸液からの重
金属類の除去法 原料としてホタテ貝に代えてホタテ貝アミノ酸液を用
い、かつ第1工程(第一洗浄)〜第7工程(油脂分離)
を省略する以外は、実施例1と同様な方法により、魚貝
類のアミノ酸液からの重金属類の除去法を実施した。そ
の結果、原料であるホタテ貝アミノ酸液に含まれるカド
ミウム検出量は3.2ppmであったが、本発明に係る
方法を実施した後、その検出量は0.08ppmまで低
下した。この結果は、肥料などの安全性を確保するため
の規制基準を大幅に下回るものである。 Example 2 Weight of fish and shellfish from amino acid solution
Metal removal method Scallop amino acid solution is used in place of scallop as raw material, and first step (first washing) to seventh step (oil and fat separation)
A method for removing heavy metals from the amino acid solution of fish and shellfish was carried out in the same manner as in Example 1 except that was omitted. As a result, the detected amount of cadmium contained in the scallop amino acid solution as a raw material was 3.2 ppm, but after the method according to the present invention was carried out, the detected amount was reduced to 0.08 ppm. This result is far below the regulatory standards for ensuring the safety of fertilizers.
【0035】実施例 3 魚貝類のアミノ酸液からの重
金属類の除去法 原料としてホタテ貝に代えてホタテ貝の中腸腺を含む内
臓塊を用い、かつ第1工程(第一洗浄)〜第4工程(p
H調製)を省略する以外は、実施例1と同様な方法によ
り、魚貝類のアミノ酸液からの重金属類の除去法を実施
した。その結果、原料であるホタテ貝の中腸腺を含む内
臓塊に含まれるカドミウム検出量は9.3ppmであっ
たが、本発明に係る方法を実施した後、その検出量は
0.12ppmまで低下した。この結果は、肥料などの
安全性を確保するための規制基準を大幅に下回るもので
ある。なお実施例におけるキレート剤等の添加量はアミ
ノ酸液に溶存するカドミウムの溶存量により変動すると
共にキレート剤の添加量によりカドミウムの除去率も変
動する。アミノ酸液に溶存するカドミウム溶存量は漁獲
される海域、時期、固体差があるため、一定ロットでサ
ンプリングし、予備テストの上キレート剤等の添加量が
決められる。 Example 3 Weight of Fish and Shellfish from Amino Acid Solution
A method for removing metals, wherein a visceral mass containing the midgut gland of the scallop is used in place of the scallop, and the first step (first washing) to the fourth step (p
Except for omitting H preparation), a method for removing heavy metals from the amino acid solution of fish and shellfish was carried out in the same manner as in Example 1. As a result, the detected amount of cadmium contained in the visceral mass including the midgut gland of the raw material scallop was 9.3 ppm, but after the method according to the present invention was carried out, the detected amount was reduced to 0.12 ppm. did. This result is far below the regulatory standards for ensuring the safety of fertilizers. In the examples, the amount of the chelating agent added varies depending on the amount of cadmium dissolved in the amino acid solution, and the cadmium removal rate also varies depending on the amount of the chelating agent added. Since the amount of cadmium dissolved in the amino acid solution varies depending on the sea area, season, and individual being caught, sampling is conducted in a fixed lot, and the amount of the chelating agent added is determined after preliminary tests.
【0036】[0036]
(1)本発明は、キレート剤に魚貝類アミノ酸液に含ま
れる重金属を吸着させて、その含有量を0.15〜0.
08ppmまで低下できる。従って本発明に係る方法に
よれば、本来厄介な産業廃棄物であるホタテ貝の中腸腺
や内臓塊含まれるカドミウムなどの重金属の含有量を肥
料などの安全性を確保するための規制基準値より大幅に
低下させることができ、単に公害の発生源を抑制できる
に止まらず、葉菜、果菜などの葉面撒布剤や潅水肥料と
して果実の糖度の向上、有機質肥料などの資源として利
用拡大できる。 (2)本発明に係る方法は、重金属の吸着剤としてキレ
ート剤を用いるため高度な技術や複雑な装置を必要とし
ない簡便な処理法である。 (3)本発明により使用するキレート剤は減圧蒸留によ
り吸着処理させたカドミウムなどの重金属を溶出させ回
収し、くり返し使用できることから、処理コストを押し
上げるげるものではない。 (4)本発明により回収されるカドミウムは原料中にp
pm単位で存在するもので微量のものであるが集積し、
精製すればカドミウムなどの重金属が本来もつ性質から
有用物として期待できる。(1) In the present invention, a heavy metal contained in a fish and shellfish amino acid solution is adsorbed to a chelating agent, and the content thereof is adjusted to 0.15 to 0.5.
It can be reduced to 08 ppm. Therefore, according to the method according to the present invention, the content of heavy metals such as cadmium contained in the midgut glands and visceral mass of scallop, which is originally a troublesome industrial waste, is regulated to ensure the safety of fertilizers and the like. Not only can the source of pollution be reduced, but also can be used as a foliar spraying agent for leafy vegetables and fruits and vegetables, as a fertilizer, to improve the sugar content of fruits, and to expand its use as a resource such as organic fertilizers. . (2) The method according to the present invention is a simple processing method that does not require advanced technology or complicated equipment because a chelating agent is used as a heavy metal adsorbent. (3) The chelating agent used in accordance with the present invention does not increase the processing cost, since heavy metals such as cadmium adsorbed by vacuum distillation are eluted and collected and can be used repeatedly. (4) Cadmium recovered by the present invention contains p
It exists in pm units and is a very small amount,
If refined, it can be expected as a useful material due to the inherent properties of heavy metals such as cadmium.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI // A23L 1/015 A23L 1/325 A 1/325 B09B 3/00 304Z (56)参考文献 特開 平3−47051(JP,A) (58)調査した分野(Int.Cl.7,DB名) B09B 3/00 A23J 3/04 501 A23L 1/238 A23L 1/015 A23L 1/325 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI // A23L 1/015 A23L 1/325 A 1/325 B09B 3/00 304Z (56) References JP-A-3-47051 (JP) , A) (58) Fields investigated (Int. Cl. 7 , DB name) B09B 3/00 A23J 3/04 501 A23L 1/238 A23L 1/015 A23L 1/325
Claims (2)
製された醗酵槽で魚貝類タンパク質を自己消化により及
び必要に応じてプロテアーゼを作用させて前記魚貝類タ
ンパク質をアミノ酸液まで分解し、次いでpHを8〜9
に調製された魚貝類アミノ酸液にキレート剤を添加し作
用させ、該キレート剤に前記魚貝類アミノ酸液に含まれ
る重金属類を吸着させることを特徴とする魚貝類アミノ
酸液から重金属類を除去する方法。1. A fish and shellfish protein is decomposed into an amino acid solution by autolyzing a fish and shellfish protein in a fermenter adjusted to a temperature of 20 to 50 ° C. at a pH of 4 or less and, if necessary, by acting a protease. , Then pH 8-9
A method for removing heavy metals from a fish and shellfish amino acid solution, comprising adding a chelating agent to the fish and shellfish amino acid solution prepared in Example 1, and allowing the chelating agent to adsorb heavy metals contained in the fish and shellfish amino acid solution. .
件で酸類を作用させて前記魚貝類タンパク質を加水分解
し、次いで20〜50℃の温度に調製された醗酵槽で魚
貝類タンパク質を自己消化により及び必要に応じてプロ
テアーゼを作用させて前記魚貝類タンパク質をアミノ酸
液まで分解し、更にpHを8〜9に調製された魚貝類ア
ミノ酸液にキレート剤を添加し作用させ、該キレート剤
に前記魚貝類アミノ酸液に含まれる重金属類を吸着させ
ることを特徴とする魚貝類アミノ酸液から重金属類を除
去する方法。2. The fish and shellfish protein is hydrolyzed by the action of acids under the condition that the pH of the crushed fish and shellfish is 4 or less, and then the fish and shellfish protein is prepared in a fermenter prepared at a temperature of 20 to 50 ° C. The fish and shellfish protein is decomposed into an amino acid solution by self-digestion and, if necessary, by the action of a protease, and a chelating agent is added to and acted on the fish and shellfish amino acid solution adjusted to a pH of 8 to 9, whereby the chelate is added. A method for removing heavy metals from a fish and shellfish amino acid solution, wherein the heavy metal contained in the fish and shellfish amino acid solution is adsorbed to an agent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24043792A JP3268657B2 (en) | 1992-09-09 | 1992-09-09 | How to remove heavy metals from amino acid solution of fish and shellfish |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24043792A JP3268657B2 (en) | 1992-09-09 | 1992-09-09 | How to remove heavy metals from amino acid solution of fish and shellfish |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06106155A JPH06106155A (en) | 1994-04-19 |
| JP3268657B2 true JP3268657B2 (en) | 2002-03-25 |
Family
ID=17059483
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24043792A Expired - Fee Related JP3268657B2 (en) | 1992-09-09 | 1992-09-09 | How to remove heavy metals from amino acid solution of fish and shellfish |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3268657B2 (en) |
Families Citing this family (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2667986B2 (en) * | 1994-09-29 | 1997-10-27 | 北海道 | Method and apparatus for removing heavy metals contained in organisms |
| JP3836231B2 (en) * | 1997-10-17 | 2006-10-25 | 日本化学飼料株式会社 | Highly unsaturated fatty acid-containing oil obtained from scallop midgut gland and method for producing the same |
| JP4698792B2 (en) * | 2000-03-17 | 2011-06-08 | 日本メナード化粧品株式会社 | Method for removing heavy metals from mushroom extract |
| JP2002336818A (en) * | 2001-05-17 | 2002-11-26 | Tamura Kagaku Kenkyusho:Kk | Mollusk food processing residue treatment method, treatment process and treatment equipment used therefor |
| JP4858828B2 (en) * | 2006-07-03 | 2012-01-18 | 亮太 篠原 | Methods for removing heavy metals from animal tissues or organs |
| JP4671203B2 (en) * | 2008-04-16 | 2011-04-13 | 石川県 | Method for removing heavy metals from fish sauce |
| JP2010057442A (en) * | 2008-09-05 | 2010-03-18 | Hokkaido Univ | Method for removing heavy metal from fish and shellfish containing harmful heavy metal in short time, and manufacturing method of foodstuff obtained by the same |
| JP5386694B2 (en) * | 2010-08-20 | 2014-01-15 | 石川県 | Method for removing heavy metals in fish sauce |
| CN102363118B (en) * | 2011-05-16 | 2013-10-09 | 浙江海洋学院 | Method for removing heavy metal lead in aquatic seasoning |
| CN102363120B (en) * | 2011-05-16 | 2013-10-09 | 浙江海洋学院 | A method for removing heavy metal copper in aquatic seasoning |
| CN102363121B (en) * | 2011-05-16 | 2013-10-09 | 浙江海洋学院 | Method for removing heavy metal chromium in aquatic seasoning |
| CN102363119B (en) * | 2011-05-16 | 2013-10-09 | 浙江海洋学院 | A method for removing heavy metal arsenic from aquatic seasoning |
| JP6122369B2 (en) * | 2013-09-24 | 2017-04-26 | 大成農材株式会社 | Method for producing organic fertilizer and organic feed |
| KR101539937B1 (en) * | 2013-11-08 | 2015-07-29 | 주식회사 삼다 | Method for making high speed fermentation eco-friendly amino acid fertilzer using by-products of aquatic products |
-
1992
- 1992-09-09 JP JP24043792A patent/JP3268657B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH06106155A (en) | 1994-04-19 |
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