JPH0461630B2 - - Google Patents
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- JPH0461630B2 JPH0461630B2 JP61006371A JP637186A JPH0461630B2 JP H0461630 B2 JPH0461630 B2 JP H0461630B2 JP 61006371 A JP61006371 A JP 61006371A JP 637186 A JP637186 A JP 637186A JP H0461630 B2 JPH0461630 B2 JP H0461630B2
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Description
(発明が属する利用分野)
本発明はカキエキス濃縮物の製法に関するもの
で、特に色調、うま味に優れ、天然調味料或いは
調味料基材乃至補助材或いは食品として有用なカ
キエキス濃縮物の製法に関する。本発明は更にこ
の方法で得られるカキエキス濃縮物にも関する。
(従来の技術)
カキエキス中には、グルタミン酸等のうま味成
分やうま味を引立てる役目をするグリコーゲン等
の各種成分が多量に含まれており、カキの缶詰を
製造する際に副生する煮汁を濃縮して得られるカ
キエキスは、所謂オイスターソース等の名称で天
然調味料として使用されている。又カキエキスは
人体の機能の回復及び維持に有効な成分を含有す
ることから、その濃縮乾燥品は健康食品として市
販されている。
(発明が解決しようとする問題点)
然しながら、カキエキスの濃縮物は黒色乃至黒
褐色の成分を比較的多量に含有しており、しよう
油やウースタソースに似た外観を呈し、着色を好
まない食品類の味付けには適さないという問題点
がある。又このような黒色乃至黒褐色の成分を含
有する濃縮物は、苦味、渋味、焦臭等の調味料と
しては望ましくない異味異臭を有し、全体として
の味がくどいものとなつている。その為従来のカ
キエキス濃縮物は所謂炒め物、焼物等の調理食品
の用途には用いられているものの、スープ、吸
物、煮物、サラダ等の味付けのあつさりした調理
食品の分野には適用されるに至つていない。
カキエキス濃縮物から前述した黒色乃至黒褐色
の着色成分を分離する方法も種々検討されたが、
これらの着色成分は液中に安定に分散しており、
吸着等の手段では分離することが困難であつた。
上記着色成分を分離除去する際に生じるもつと
も重要な問題は、カキエキス中に含まれるうま味
成分或いは栄養成分を減少させてはならないとい
うことであり、この要求に応える吸着剤等の精製
剤もいまだみいだされるに至つていない。従つ
て、本発明の技術的課題は上記欠点が解消された
カキエキス濃縮物及びその製法を提供するにあ
る。
(問題点を解決するための手段)
本発明によれば固形分濃度が30重量%以下のカ
キエキス液に比表面積が50m2/g以上の水不溶性
無機マグネシウム化合物を主体とする吸着剤を作
用させて吸着精製処理を行い、次いで精製液を実
質上非酸化雰囲気中で固形分濃度が5重量%以上
となるように濃縮する。
(作用)
本発明者等は本発明に到達する過程で次に述べ
る興味のある事実を見出した。カキエキスを濃縮
していくと固形分濃度の低い初期の段階では黒色
乃至黒褐色の着色成分は殆んど無いか或いは有る
としても少なく、酸化性雰囲気の下では濃縮が進
行して固形分濃度が10重量%以上と高くなるにつ
れてその含有量が著しく増大し非酸化性雰囲気中
でも固形分濃度30重量%以上となる著しく着色す
る。このように着色成分の含有量が増大すると、
吸着処理等の通常の精製手段ではこれを除去する
ことが困難であることは既に前述した通りであ
る。上述した事実はカキエキス中に含有される複
数の成分が濃縮過程中に相互に反応乃至縮合した
比較的高分子量の着色成分を生ずるに至るものと
推定され、このことは一般に多くの食品の加工・
保存においてメイラード反応といわれアミノ酸、
アミン、蛋白質などのアミノ基をもつアミノ化合
物と糖及びカルボニル化合物との間に起こる褐変
反応乃至黒変反応と思われ、もつとも重要なのは
還元糖で食品類の加熱加工に際して反応性が高ま
り、特に食品の加工・保存においてこの還元糖に
起因するメイラード反応は、食品の栄養化、うま
味及び味の低下乃至変質を来たすことから問題と
なる。本発明は、この着色成分が多量に生ずる以
前の段階においてカキエキス液に比表面積が50
m2/g以上の無機マグネシウム化合物、例えば層
状フイロケイ酸マグネシウムを主体とする吸着剤
を作用させると、黒色乃至黒褐色の着色物質の前
駆物質の除去が、うま味成分や栄養物質の含有量
を大きく低減させること無しに、効果的に除去で
きるという知見に基づくものである。
本発明によればこのように着色物質の原因とな
る前駆物質が除去されている為この精製液を高濃
度に濃縮する場合にも着色物質が生成すること無
く、色調、うま味及びフレーバーの組合せの優れ
た濃縮物が得られるものである。
本発明において前述した無機マグネシウム化合
物が特異的に着色物質の前駆物質を吸着除去する
理由は未だ解明されるに至つていないが、物理吸
着の他に化学吸着(イオン吸着も含む)も関係し
更には前述した褐変反応そのものを抑制している
ものと思われる。この三者が関連していること
は、濃縮中に生成した着色成分そのものに対して
は水不溶性無機マグネシウム化合物がかなり低い
吸着性しか示さないという事実とも良く符合して
いる。
(発明の作用効果)
本発明によるカキエキス濃縮物は、黒色乃至黒
褐色の着色成分を含有せず、淡黄色乃至コハク色
の外観を呈し、任意の食品類に対する味付け等の
目的に広く使用し得ると共に、苦味、渋味、焦臭
等の異味異臭が除去されカキ本来の上品でまろや
かな繊細なうま味、風味が強調されている為、ス
ープ、吸物、煮物、焼物、サラダ、珍味類、菓
子、飲料等を含めてその他のすべての調理食品、
加工食品等に対する天然調味料或いは調味料基材
乃至助材として使用することができる。又風味が
良く喫飲性に優れていることから、それ自体で健
康食品、栄養補給食品等の用途にも使用される。
又本発明の方法は、カキエキス濃縮過程の中間
の段階でカキエキスと前述した吸着剤を接触させ
れば良く、格別面到な精製処理を必要としないこ
とから操作が簡単であり処理コストも比較的低く
てすむという方法上の利点がある。
(発明の好適実施態様の説明)
処理に用いるカキエキスとしてはカキの煮汁あ
るいはその部分濃縮物が有利に使用される。この
原料カキエキス液は一般に2乃至30重量%、特に
3乃至15重量%の固形分濃度を有するものが良
い。濃度が上記範囲を超えると原料エキス中に黒
色乃至黒褐色の着色成分の含有量が増加するので
望ましくなく、上記範囲よりも低いと多量の液を
取り扱わねばならないことから経済的に不利であ
る。カキエキス原料としては上に示したものの
他、カキの身の摺砕物を熱と水との作用下に処理
して得られるエキスももちろん使用できる。勿
論、原液エキスをイオン交換膜を用いて脱塩操作
に付して得られる脱塩原液エキスを用いることも
できる。
一例として乾燥カキエキスの成分表を第1表に
示す。
第1表
一般成分
カロリー ……354cal
水 分 ……2.6g
たんぱく質 ……38.1g
脂 質 0.2g
灰 分 ……9.2g
繊 維 ……0g
炭水化物(糖質) 49.9g
アミノ酸組成
必須アミノ酸類
イソロイシン ……0.96g
ロイシン ……1.56g
リジン ……1.98g
メチオニン ……0.63g
フエニルアラニン ……0.86g
スレオニン ……1.30g
トリプトフアン ……0.22g
バリン ……1.24g
システイン ……0.36g
チロシン ……0.74g
アルギニン ……1.82g
ヒスチジン ……0.63g
アラニン ……1.85g
アスパラギン酸 ……2.98g
グルタミン酸 ……4.25g
グリシン ……1.95g
プロリン ……2.53g
セリン ……1.15g
無機質
カルシウム ……115mg
リン ……552mg
マンガン ……2.28mg
マグネシウム 241mg
ナトリウム 1860mg
カリウム 1410mg
コバルト 14μg
鉄 ……5.30mg
銅 ……1.9mg
亜 鉛 ……40.2mg
ヨウ素 ……0.6mg
ビタミン類
ビタミンB2 ……1.67mg
ビタミンB6 ……0.43mg
ビタミンB12 ……34μg
ビタミンH(ビオチン) ……27μg
イノシトール ……93mg
コリン 280mg
有用成分
タウリン ……4.2g
グリコーゲン ……27g
リン脂質 ……10mg
本発明に於いては比表面積が50m2/g以上、特
に100乃至800m2/gの範囲にある水不溶性無機マ
グネシウム化合物を主体とする吸着剤を使用す
る。比表面積が上記範囲よりも小さい化合物では
着色成分の前駆物質に対する吸着能が本発明のも
のに比して劣る。この無機マグネシウム化合物は
実質上水に不溶であることも重要であり、水溶性
のものでは濃縮物の風味の点で好ましくない。
本発明に用いられる水不溶性でかつ吸着性能の
大きい無機マグネシウム化合物としては、マグネ
シウムのケイ酸塩、炭酸塩、部分酸付加物、部分
水酸化物等のうち、低結晶質で比表面積の高いも
のが好ましい。
特に、ケイ酸分とマグネシウムの酸化物及び/
又は水酸化物を水熱処理することによつて得ら
れ、下記式
MgO・mSiO2・nH2O
但し、0.5≦m≦2、n≦2
の組成を有し、且つ100m2/g以上の比表面積を
有するケイ酸マグネシウムがより好適に用いら
れ、中でも上記組成式でm=4/3のケイ酸マグネ
シウムが最も好適である。
本発明に最も好適に用いられる上記組成(m=
4/3)のケイ酸マグネシウムは、下記構造式
〔Mg3〕(Si2O5)2(OH)2
・xH2O(x≦5)
によつても表わされ、面間隔4.5〜4.6Å、2.5〜
2.6Å及び1.5〜1.6Åにx線回折ピークを有し、且
つ300m2/g以上の比表面積を有する層状のフイ
ロケイ酸マグネシウムから成る水不溶性の鉱物性
物質である。該層状フイロケイ酸塩鉱物の合成
は、ケイ酸分原料として合成ケイ酸、天然ケイ
ソウ土、フエロシリコンダスト等の非晶質シリ
カ、ケイソウ土焼成物、硅石等の結晶質シリ
カ、粘土鉱物等の酸処理によつて得られる活性
ケイ酸乃至活性アルミノケイ酸、又は反応条件
下にシリカを形成し得る化合物を用い、マグネシ
ウム原料としては、マグネシウムの酸化物、水酸
化物又は反応条件下に前記酸化物乃至水酸化物を
形成し得る化合物を用いて、両者を水性媒体中で
混合し、スラリー状となし、常圧下又は加圧下に
水熱処理することにより達成される。反応条件と
しては80乃至200℃の温度が使用され、この場合、
反応系の圧力は0.5乃至16Kg/cm2に維持され、反
応時間は温度及び圧力によつても相違するが0.5
乃至10時間の範囲が適当である。生成物は、必要
により水洗し、乾燥、粉砕、分級等の後処理を行
なつて水不溶性の白色粉末状吸着剤に製すること
が出来る。
かくして得られる合成層状フイロケイ酸マグネ
シウムは、前記の構造式
〔Mg3〕(Si2O5)2(OH)2
・xH2O(x≦5)
からも推考できるように、天然の粘土鉱物である
タルク(滑石)に類似した構造、すなわちMgO6
の八面体層(ブルーサイト層)を間に挟んで2つ
のSiO4の四面体層(フイロケイ酸層)がンドイ
ツチされた三層構造のものを主体としており、こ
の層状構造に特有のx線回折スペクトルを有す
る。第1図は本発明に最も好適に用いられる合成
層状フイロケイ酸マグネシウムのx線回折図であ
り、面間隔4.5〜4.6Å(〔0.20〕面、〔110〕面に対
応)、2.5〜2.6Å(〔200〕面に対応)、及び1.5〜
1.6Å(〔060〕面に対応)に夫々回折ピークを有
することが明らかであり、これは天然のトリオク
タヘドラル型層状粘土鉱物に共通のx線回折ピー
クである。
本発明に用いる合成層状フイロケイ酸マグネシ
ウムは、タルク等天然のフイロケイ酸塩には全く
認められなかつた極めて大きな比表面積と吸着力
を有する。これは、合成層状フイロケイ酸マグネ
シウムでは、x線回折ピークのブロードな形状か
ら分るように低結晶質であることに由来し、結晶
子が微細であることと、層の積み重ねに不規則性
があり、この層間に他の物質が入り易い構造とな
つているためと思われる。
本発明に用いる無機マグネシウム化合物を主体
とする吸着剤は、粉状のままで用いても良いが、
吸着処理後の固液分離を容易にする目的で、予め
吸着剤粉末を水及び必要に応じて水不溶性の粘結
性鉱物すなわち酸性白土、白陶土(カオリン)又
はベントナイト等とともに成形し、乾燥又は仮焼
により固結させて粒状等の成形体として用いるこ
とも出来る。無機マグネシウム化合物はカキエキ
ス当り0.5乃至20重量%特に1乃至15重量%の量
で添加するのが良い。上記範囲よりも低いと着色
物質の前駆物質の除去が不十分であり、上記範囲
より多いとうま味成分や栄養成分の実質的な量が
吸着除去されるようになり、本発明の目的に好ま
しくない。
本発明に於いては上記無機マグネシウム化合物
を単独で吸着剤として使用する他、活性白土、酸
性白土、シリカ、アルミナ、シリカアルミナ、ゼ
オライト、活性炭等の他の吸着剤と組合せて使用
することができる。
本発明者等は無機マグネシウム化合物と活性炭
との組合せで使用すると、うま味成分等の含有量
をあまり低減させることなく、着色成分の前駆物
質を最も効果的に吸着除去できることを見い出し
た。無機マグネシウム化合物を単独で使用する場
合には着色成分の前駆物質を完全に除去するには
かなり多量に使用しなければならず、それに伴つ
てうま味成分等の吸着もかなり生ずるようにな
る。活性炭は着色成分の前駆物質の除去にかなり
有効であるけれどうま味成分等を同時に吸着して
その含有量を著しく低減させることが致命的な欠
点である。この両者を組合せて使用すると、うま
味成分等をあまり低減させることなく着色成分の
前駆物質を有効に除去できるようになる。この場
合無機マグネシウム化合物は0.5乃至20重量%特
に1乃至15重量%、活性炭は0.1乃至5重量%特
に0.2乃至3重量%の量で使用するのが良く両者
の重量比は2:1乃至10:1とするのが最も良
い。無機マグネシウム化合物と活性炭とは同時に
原料カキエキスに接触させるのが最も良いが、最
初に活性炭と接触させ次いでマグネシウム化合物
と接触させることあるいは逆の順序に接触させる
ことも可能である。
原料カキエキスと吸着剤との接触条件は前記成
分が吸着除去されるようなものであれば良く、格
別の制限はないが、一般に0乃至100℃の温度で
1分間以上接触させるのが良く、室温での処理が
特に有利である。吸着処理はカキエキス中に吸着
剤の粉末を投入し所定時間撹拌後濾過分離する方
法や、吸着剤を充填した塔にカキエキスを通し吸
着処理を行なう方法などそれ自体公知の任意の吸
着精製手段を適用できる。
吸着処理を終えた精製液を実質上非酸化性の雰
囲気中で固形分濃度が5重量%以上となるように
濃縮する。濃縮に際しては可及的に低温で水分の
蒸発が有効に行なわれることが望ましく、このた
め減圧乃至真空濃縮が望ましい。溶剤を使用する
共沸蒸溜ももちろん可能である。又窒素等の不活
性ガスをキヤリアガスとする蒸発濃縮も可能であ
る。濃縮を効率良く行なうために多段濃縮缶を用
いることもできる。
濃縮物として粘稠な液体乃至ペースト状の製品
とすることもできるし、更に凍結乾燥、噴霧乾燥
等の乾燥手段を適用して粉末粒状物等の製品とす
ることもできる。又それ自体の粘結性を利用し
て、あるいは他の食品質バインダー、例えば多糖
類を使用して板状、フレーク状あるいはケーキ状
の成形品とすることもできる。
本発明によればカキエキスの脱色濃縮物であつ
て、必須成分としてアミノ酸、たんぱく質、糖類
及び各種ミネラル分を含有し、5重量%以上の固
形分を含有し、且つ下記式
S=∫800 400ε(x)dx
式中ε(x)は固形分濃度5重量%の溶液につい
て、厚さ10〓のセルを用いて測定した時の波長x
ナノメータに於ける吸光度を表わす。
で定義される吸光度積分値Sが200以下であるこ
とを特徴とするカキエキス脱色濃縮物が提供され
る。
上述した吸光度積分値Sは可視波長域400乃至
800ナノメータの範囲に吸収を有する全物質の光
学的積算量を意味し、液の透明性とは逆の関係に
ある数値である。従来のカキエキス濃縮物は一般
に400以上の吸光度積分値Sを有し、又部分濃縮
物でも一般に250以上の吸光度積分値を示すのに
対して、本発明による精製液は200以下の吸光度
積分値を示し、固形分濃度が40重量%以上となる
ように濃縮した場合でも150以下の吸光度積分値
を示すにすぎない。
第2図は原料エキス及び従来法による濃縮物の
可視部吸収スペクトルを示し、第3図は本発明に
よる精製カキエキス及びその濃縮物の可視部吸収
スペクトルを示す。これらの比較から本発明によ
る濃縮物では短波長側に吸収を有する成分の含有
量が著しく減少しているとともに濃縮によるその
増大も顕著に抑制されていることがわかる。
本発明による濃縮物では、このように着色成分
が除去され、又それに基づく異味異臭成分が除去
されていることが顕著な特徴であるが、カキエキ
ス中のうま味成分や風味成分が高度に濃縮された
形で存在していることも顕著な特徴である。
本発明によるカキエキス濃縮物が上品でまろや
かでしかも繊細なうま味及び風味を有する事実は
結局のところ後述する例に示す通り官能試験によ
らざるを得ないが、本発明によるカキエキス濃縮
物が前述した好ましくない成分以外の有効成分を
高濃度で含有している事実はそのクロマトグラム
を参照することにより明らかである。添付図面第
4図及び第5図は、カキエキス原液について、活
性炭単独を使用して吸光度積分値がほぼ70となる
ように処理した精製液(第4図)、及び層状フイ
ロケイ酸マグネシウムと活性炭との組合せを使用
して吸光度積分値が上記と同じ値となるように処
理した精製液(第5図)について固形分濃度が5
重量%となるように調製し水を展開液及び東洋曹
達工業株式会社製ゲルG2500PWXLをカラムとし
て使用した高速液体クロマトグラフイーにおける
クロマトグラムを示す。これらの比較から本発明
による濃縮物ではカキエキス中の有効成分がより
高濃度に保有されているという事実が明らかであ
る。第5図のクロマトグラムにおいてピークEは
ロイシン及び/又はイソロイシンに固有のピーク
でありピークFはグルタミン酸及び/又はコハク
酸に特有のピークであり、ピークG及びHはその
他のうま味成分(他のアミノ酸及び/又は水溶性
低分子量蛋白質成分と思われる)に基づくピーク
であるがこれらのピークは第4図の場合に比して
顕著に高いことが注目されるべきであろう。
又本発明は更にこの方法で得られるカキエキス
の他に、鰹(カツオ)、鯖(サバ)、鯛(タイ)、
鯵(アジ)、鰤(ブリ)、ほたて貝、海老、蟹等の
魚介甲殻類、こんぶ等の海草類、チキンガラ、白
菜等の野菜類、マムシ等の爬虫類及びスツポン等
の亀甲類等のエキスにも利用されるし、更には本
発明に用いたカキエキスに前述したエキス類を混
合させた複合エキスに対しても本発明の方法を用
いることによつて同様に脱色濃縮物とすることが
出来る。
(実施例)
本発明を次の例で説明する。
本実施例中における各特性の試験方法はつぎの
とおりである。
(1) 吸着剤の比表面積測定方法
自動BET(比表面積)測定装置(Carlo
Erba社製Sorptomatic Series1800)により測
定する。
(2) カキエキス固形分濃度測定方法
試料カキエキス中の不溶分、夾雑物をNo.5C
定量濾紙で濾過分離し、濾液を供試液とした。
供試液約1gを重量既知の直径約4cmのガラス
秤量瓶(ag)に採取し、その重量(bg)を
精秤する。それを105℃に調整した恒温乾燥器
に入れ5時間乾燥して恒量となす。デシケータ
ーにて放冷後その重量(cg)を精秤する。
固形分濃度(重量%)を次式により算出す
る。
固形分濃度(重量%)=(c−a)/(b−a)×
100
(3) カキエキス吸光度積分値(S)測定方法
あらかじめ不溶分、夾雑物を分離し、固形分
濃度既知の試料カキエキスを蒸溜水で固形分濃
度5重量%に希釈し供試液とした。
供試液の波長400ナノメータから800ナノメー
タ間の吸光スペクトルを自動記録式分光光度計
(日本分光工業製ダブルビーム・ダブルモノク
ロメータ分光光度計UVIDEC650)を用いて次
の条件で得る。
標準(対照光路):蒸溜水
スペクトル幅:2.00nm
時定数:0.4秒
波長走査範囲:800〜400nm
波長スケール:40nm/cm3
測定スケール:0.000〜5.000吸光度
使用セル:10m/m石英セル
吸光度積分値(S)は下記式で表わされるが
S=∫800 400ε(x)dx
式中ε(x)は固形分濃度5重量%の溶液につい
て、厚さ10〓のセルを用いて測定した時の波長
xナノメータに於ける吸光度を表わし、吸光度
積分値(S)の算出は吸収スペクトル図の積分域面
積測定により求める。
(4) 高速液体クロマトグラフイーによるクロマト
グラム測定方法
あらかじめ不溶分、夾雑物を分離し、固形分
濃度既知の試料カキエキスを蒸溜水で固形分濃
度5重量%に希釈し供試液とする。
供試液のクロマトグラムを高速液体クロマト
グラフイー装置(日本ウオーターズリミテツド
社製)を用いて次の条件で測定する。
カラム:水酸基含有架橋ビニル重合体ゲル(東洋
曹達工業株式会社製ゲル(G2500 PWXL)
展開液:水
流 速:0.8ml/分
注入量:10μ
圧 力:300〜350PSI
温 度:20℃
検出器:UV(254nm1.0AUFS)
記録計フルスケール:10mV
(5) カキエキス風味試験方法
試料カキエキス濃縮物及び固形分5重量%に
希釈したカキエキスを供試液とした。
供試液の風味をよく訓練された10名の調理関
係者に10点満点法で評価してもらい、平均点で
表わした。
実施例 1
カキの煮汁(固形分6.2重量%)1200gをステ
ンレス容器にとり、639m2/gの比表面積を有す
る合成層状フイロケイ酸マグネシウム(水沢化学
工業製商品名ミズカナイト)60gを加えて30℃の
温度で30分間かきまぜたものを、No.5C定量濾紙
を用いて濾過し、淡黄色の透明なカキエキス液を
得た(第1工程)。
次に第1工程にて得たカキエキス液1000gを2
のナス型フラスコにとり、ロータリーエバポレ
ーター(ヤマト科学製RE46A型)を用い、減圧
下90℃の温度で濃縮し、140gの粘稠なコハク色
を有するカキエキス濃縮物を得た(第2工程)。
本品の固形分濃度を測定したところ43重量%の
濃度であつた。又本品を蒸溜水を用いて5重量%
の濃度に希釈したものの吸光スペクトルにより算
出した吸光度積分値S、第5図に示した高速液体
クロマトグラフイーによるクロマトグラムとの比
較結果、風味試験結果は第2表に示したとおりで
あり、カキエキス濃縮物として極めて優れた商品
価値を有するものであつた。
実施例 2
カキの煮汁(固形分6.2重量%)1300gをステ
ンレス容器にとり、184m2/gの比表面積を有す
る試薬ケイ酸マグネシウム(和光純薬製)195g
を加えて30℃の温度で30分間かきまぜたものをNo.
5C定量濾紙を用いて濾過し、淡黄色の透明なカ
キエキス液を得た(第1工程)。
次に第1工程にて得たカキエキス液1000gを2
のナス型フラスコにとり、ロータリーエバポレ
ーターを用い、減圧下90℃の温度で濃縮し、158
gの粘稠なコハク色を有するカキエキス濃縮物を
得た(第2工程)。
本品の固形分を測定したところ38重量%の濃度
であつた。又本品の吸光度積分値S、クロマトグ
ラム比較結果、風味試験結果は第2表に示したと
おりであり、カキエキス濃縮物として極めて優れ
た商品価値を有するものであつた。
実施例 3
合成層状フイロケイ酸マグネシウムと活性炭を
重量比3:1の割合で混合し、水の存在下で複合
化反応を行ない、濾過、乾燥、粉砕の後処理を行
なつて、比表面積540m2/gを有する複合吸着剤
粉末を得た。
次にカキの煮汁(固形分濃度6.2重量%)1200
gをステンレス容器にとり、得られた複合吸着剤
粉末25gを加え、30℃の温度で30分間かきまぜた
ものをNo.5C定量瀘紙を用いて濾過し、淡黄色の
透明なカキエキス液を得た(第1工程)。
次に第2工程にて得たカキエキス液1000gを2
のナス型フラスコにとり、ロータリーエバポレ
ーターを用い、減圧下90℃の温度で濃縮し、133
gの粘稠なコハク色を有するカキエキス濃縮物を
得た(第2工程)。
本品の固形分濃度を測定したところ45重量%の
濃度であつた。又本品の吸光度積分値S、クロマ
トグラム比較結果、風味試験結果は第2表に示し
たとおりであり、カキエキス濃縮物として極めて
優れた商品価値を有するものであつた。
実施例 4
カキの煮汁(固形分6.2重量%)1200gをステ
ンレス容器にとり、639m2/gの比表面積を有す
る合成層状フイロケイ酸マグネシウム(水沢化学
工業製ミズカナイト)18gと、活性炭(武田薬品
工業製強力白鷺)6gを加えて30℃の温度で30分
間かきまぜたものをNo.5C定量濾紙を用いて濾過
し淡黄色の透明なカキエキス液を得た(第1工
程)。
次に第1工程にて得たカキエキス液1000gを2
のナス型フラスコにとり、ロータリーエバポレ
ーターを用い、減圧下90℃の温度で濃縮し、154
gの粘稠なコハク色を有するカキエキス濃縮物を
得た(第2工程)。
本品の固形分を測定したところ39重量%の濃度
であつた。又本品の吸光度積分値S、クロマトグ
ラム比較結果、風味試験結果は第2表に示したと
おりであり、カキエキス濃縮物として極めて優れ
た商品価値を有するものであつた。
実施例 5
カキの煮汁(固形分6.2重量%)1200gをステ
ンレス容器にとり、168m2/gの比表面積を有す
る合成ハイドロタルサイト60gと活性炭(武田薬
品工業製カルボラフイン)7.2gを加えて30℃の
温度で30分間かきまぜたものをNo.5C定量濾紙を
用いて濾過し、淡黄色の透明なカキエキス液を得
た(第1工程)。
次に第1工程にて得たカキエキス液1000gを2
のナス型フラスコにとり、ロータリーエバポレ
ーターを用い、減圧下90℃の温度で濃縮し、143
gの粘稠なコハク色を有するカキエキス濃縮物を
得た(第2工程)。
本品の固形分を測定したところ42重量%の濃度
であつた。又本品の吸光度積分値S、クロマトグ
ラム比較結果、風味試験結果は第2表に示したと
おりであり、カキエキス濃縮物として極めて優れ
た商品価値を有するものであつた。
実施例 6
実施例3の第2工程にて得たカキエキス濃縮物
100gを直径30cmのガラス皿にとり、105℃に調整
した恒温乾燥器に入れ8時間乾燥しカキエキス固
形品を得た。この固形品を卓上型サンプルミルに
て粉砕し、コハク色を有するカキエキス粉末を得
た。
本カキエキス粉末を蒸溜水を用いて5重量%の
濃度になるように溶解したものの吸光スペクトル
より算出した吸光度積分値S、クロマトグラム比
較結果、風味試験結果は第2表に示したとおりで
あり、カキエキス粉末として極めて優れたもので
あつた。
実施例 7
カキの煮汁(固形分6.2重量%)1200gを2
のナス型フラスコにとり、639m2/gの比表面積
を有する合成層状フイロケイ酸マグネシウム(水
沢化学工業製ミズナイト)18gと、活性炭(武田
薬品工業製強力白鷺)6gを加えて、ロータリー
エバポレーターを用い、減圧下90℃の温度で濃縮
し、吸着剤を含む211gの粘稠なカキエキス濃縮
物を得た(第1工程)。
次に第1工程にて得たカキエキス濃縮物を小型
遠心分離機(5000G)を用いて吸着剤を分離除去
し165gの粘稠なコハク色を有するカキエキス濃
縮物を得た(第2工程)。
本品の固形分濃度を測定したところ41重量%の
濃度であつた。又本品の吸光度積分値S、クロマ
トグラム比較結果、風味試験結果は第2表に示し
たとおりであり、カキエキス濃縮物として極めて
優れた商品価値を有するものであつた。
実施例 8
カキの煮汁(固形分6.2重量%)1200gを2
のナス型フラスコにとり、ロータリーエバポレー
ターを用い、減圧下80℃の温度で濃縮し、300g
の不透明な茶色のカキエキス部分濃縮物を得た
(第1工程)。
次に第1工程にて得た部分濃縮物300gに639
m2/gの比表面積を有する合成層状フイロケイ酸
マグネシウム(水沢化学工業製ミズカナイト)18
gと活性炭(武田薬品工業製強力白鷺)6gをエ
バポレーターの真空圧を常圧に戻してからすぐに
加えて、30℃の温度で60分間かきまぜたものを、
小型遠心分離機(5000G)を用いて吸着剤を分離
除去し、コハク色を有し、固形分濃度25重量%の
カキエキス部分濃縮物260gを得た(第2工程)。
次に第2工程にて得た精製部分濃縮カキエキス
液250gを1のナス型フラスコにとり、ロータ
リーエバポレーターを用いて、減圧下90℃の温度
で濃縮し、152gの粘稠なコハク色を有するカキ
エキス濃縮物を得た(第3工程)。
本品の固形分濃度を測定したところ41重量%の
濃度であつた。又本品の吸光度積分値S、クロマ
トグラム比較結果、風味試験結果は第2表に示し
たとおりであり、カキエキス濃縮物として極めて
優れた商品価値を有するものであつた。
比較例 1
カキの煮汁(固形分6.2重量%)を吸着剤を加
えることなしにNo.5C定量濾紙を用いて濾過し、
不溶分、夾雑物を除去したカキエキス原液を得た
(第1工程)。
次に第1工程にて得たカキエキス液1000gを2
のナス型フラスコにとり、ロータリーエバポレ
ーターを用い、減圧下90℃の温度で濃縮し、144
gの粘稠な黒褐色のカキエキス濃縮物を得た(第
2工程)。
本品の固形分濃度を測定したところ43重量%の
濃度であつた。又本品の吸光度積分値S、クロマ
トグラム比較結果、風味試験結果は第2表に示し
たとおりであり、黒色の強い着色がひどく、異味
異臭も有し、風味に欠けるものであつた。
比較例 2
カキの煮汁(固形分6.2重量%)1200gをステ
ンレス容器にとり、活性炭(武田薬品工業製強力
白鷺)6gを加えて30℃の温度で30分間かきまぜ
たものを、No.5C定量濾紙を用いて濾過し、更に
遠心分離機(5000G)にて濾過洩れの活性炭を分
離し、やや黒味のある淡黄色の透明なカキエキス
液を得た(第1工程)。
次に第1工程にて得たカキエキス液1000gを2
のナス型フラスコにとり、ロータリーエバポレ
ーターを用い減圧下90℃の温度で濃縮し、150g
の粘稠な黒褐色を有するカキエキス濃縮物を得た
(第2工程)。
本品の固形分濃度を測定したところ40重量%の
濃度であつた。又本品の吸光度積分値S、クロマ
トグラム比較結果、風味試験結果は第2表に示し
たとおりであり、着色が強く、やや風味にも欠
け、商品価値において劣るものであつた。
比較例 3
カキの煮汁(固形分6.2重量%)1200gをステ
ンレス容器にとり、活性炭(武田薬品工業製強力
白鷺)15gを加えて30℃の温度で30分間かきまぜ
たものを、No.5Cの定量濾紙を用いて濾過し、更
に遠心分離機(5000G)にて濾過洩れの活性炭を
分離し、僅かに黄色味のある透明なカキエキス液
を得た(第1工程)。
次に第1工程にて得たカキエキス液1000gを2
のナス型フラスコにとり、ロータリーエバポレ
ーターを用い、減圧下90℃の温度で濃縮し、158
gの粘稠なコハク色を有するカキエキス濃縮物を
得た(第2工程)。
本品の固形分濃度を測定したところ38重量%の
濃度であつた。又本品の吸光度積分値S、クロマ
トグラム比較結果、風味試験結果は第2表に示し
たとおりであり、着色は少ないがうま味、風味に
欠けるものであつた。
比較例 4
カキの煮汁(固形分6.2重量%)1200gを1
のナス型フラスコにとり、ロータリーエバポレー
ターを用い、減圧下90℃の温度で濃縮し、230g
の粘稠な黒褐色を有する固形分濃度35重量%のカ
キエキス濃縮物を得た(第1工程)。
次に第1工程にて得たカキエキス濃縮物200g
をステンレス容器にとり、639m2/gの比表面積
を有する合成層状フイロケイ酸マグネシウム(水
沢化学工業製ミズナイト)19g、活性炭(武田薬
品工業製強力白鷺)19gを加えて20℃の温度で30
分間かきまぜたものを小型遠心分離機(5000G)
を用いて吸着剤を分離除去し、黒褐色のカキエキ
ス濃縮物を得た(第2工程)。
本品の固形分濃度を測定したとこ31重量%の濃
度であつた。本品の吸光度積分値S、クロマトグ
ラム比較結果、風味試験結果は第2表に示したと
おりであり、黒味の強い着色がひどく、異味異臭
も有し、風味に欠けるものであつた。
比較例 5
市販の濃縮カキエキス(香港産オイスターソー
ス)100gを蒸溜水100gを用いて希釈し、固形分
濃度21重量%の希釈液を得た。この希釈液を遠心
分離機(5000G)を用いて不溶分、夾雑物を分離
したら固形分16重量%の褐色を有する透明なカキ
ソース液を得た。又遠心分離の際の残渣は多量の
ペースト状でん粉であつた。
希釈、遠心分離した本カキエキス液を蒸溜水を
用いて5重量%の濃度に希釈したものの吸光スペ
クトルより算出した吸光度積分値S、クロマトグ
ラム比較結果、風味試験結果は第2表に示したと
おりであり、カキエキス液としては着色が強く、
風味もややものたりないものであつた。
(Field of Application to which the Invention Pertains) The present invention relates to a method for producing a oyster extract concentrate, and particularly to a method for producing a oyster extract concentrate that has excellent color tone and flavor and is useful as a natural seasoning, a seasoning base or auxiliary material, or as a food. The invention further relates to the persimmon extract concentrate obtained by this method. (Prior technology) Oyster extract contains large amounts of umami components such as glutamic acid and various components such as glycogen, which enhances the umami flavor, and concentrates the broth that is a by-product when producing canned oysters. The obtained oyster extract is used as a natural seasoning under the name of so-called oyster sauce. Moreover, since oyster extract contains ingredients effective in restoring and maintaining the functions of the human body, its concentrated dried product is commercially available as a health food. (Problem to be Solved by the Invention) However, oyster extract concentrate contains a relatively large amount of black or blackish-brown components, and has an appearance similar to soy sauce or Worcester sauce, making it difficult to use in food products that do not like coloring. The problem is that it is not suitable for seasoning. Concentrates containing such black or dark brown components have unpleasant tastes and odors such as bitterness, astringency, and burnt odor, which are undesirable as seasonings, and the overall taste is unpleasant. For this reason, conventional oyster extract concentrates are used for so-called cooked foods such as stir-fried foods and grilled foods, but they are also used for seasoned cooked foods such as soups, soups, stews, and salads. has not yet been reached. Various methods have been studied to separate the aforementioned black or blackish-brown coloring components from oyster extract concentrate; however,
These coloring components are stably dispersed in the liquid,
It was difficult to separate by means such as adsorption. The most important problem that arises when separating and removing the above-mentioned colored components is that the umami or nutritional components contained in the oyster extract must not be reduced, and there are still no purification agents such as adsorbents that meet this requirement. It has not yet been released. Therefore, the technical problem of the present invention is to provide a persimmon extract concentrate and a method for producing the same, which eliminate the above-mentioned drawbacks. (Means for solving the problem) According to the present invention, an adsorbent mainly composed of a water-insoluble inorganic magnesium compound having a specific surface area of 50 m 2 /g or more is applied to a persimmon extract liquid having a solid content concentration of 30% by weight or less. Then, the purified liquid is concentrated in a substantially non-oxidizing atmosphere to a solid content concentration of 5% by weight or more. (Function) The present inventors discovered the following interesting fact in the process of arriving at the present invention. When oyster extract is concentrated, at the initial stage when the solid content concentration is low, there are almost no black or blackish brown coloring components, or if there are any, there are few, but in an oxidizing atmosphere, concentration progresses and the solid content concentration reaches 10%. As the content becomes higher than 30% by weight, the content increases significantly, and even in a non-oxidizing atmosphere, the solid content becomes 30% by weight or more, resulting in significant coloration. When the content of coloring components increases in this way,
As already mentioned above, it is difficult to remove this by ordinary purification means such as adsorption treatment. The above-mentioned fact suggests that the multiple components contained in oyster extract react or condense with each other during the concentration process, resulting in relatively high molecular weight coloring components.
Amino acids are preserved in what is called the Maillard reaction.
It is thought to be a browning or blackening reaction that occurs between amino compounds with amino groups, such as amines and proteins, and sugars and carbonyl compounds, and the most important one is reducing sugars, which increase reactivity during heat processing of foods. In the processing and preservation of food products, the Maillard reaction caused by reducing sugars poses a problem because it causes a decrease or alteration in the nutritional value, umami, and taste of foods. In the present invention, the oyster extract liquid has a specific surface area of 50
When an adsorbent based on an inorganic magnesium compound of m 2 /g or more, such as layered magnesium phyllosilicate, is used, the precursors of black to dark brown coloring substances are removed, and the content of umami components and nutritional substances is greatly reduced. This is based on the knowledge that it can be effectively removed without causing any damage. According to the present invention, since the precursor substances that cause colored substances are removed, even when this purified liquid is concentrated to a high concentration, colored substances are not generated, and the combination of color tone, umami, and flavor can be improved. An excellent concentrate is obtained. The reason why the inorganic magnesium compound mentioned above specifically adsorbs and removes the precursor of the colored substance in the present invention has not yet been elucidated, but in addition to physical adsorption, chemical adsorption (including ion adsorption) is also involved. Furthermore, it seems that the browning reaction itself mentioned above is suppressed. The fact that these three are related is in good agreement with the fact that water-insoluble inorganic magnesium compounds exhibit only a fairly low adsorption to the colored components themselves generated during concentration. (Actions and Effects of the Invention) The oyster extract concentrate according to the present invention does not contain black or blackish-brown coloring components, has a pale yellow to amber appearance, and can be widely used for purposes such as seasoning any food. It removes off-flavors such as bitterness, astringency, and burnt odor, and emphasizes the elegant, mellow, delicate umami and flavor of oysters, making them ideal for soups, soups, boiled dishes, grilled dishes, salads, delicacies, sweets, and beverages. All other prepared foods, including
It can be used as a natural seasoning for processed foods, or as a seasoning base material or auxiliary material. In addition, since it has a good flavor and is easy to drink, it is also used as a health food, nutritional supplement food, etc. In addition, the method of the present invention requires only contacting the oyster extract with the above-mentioned adsorbent at an intermediate stage of the oyster extract concentration process, and does not require any special purification treatment, so the operation is simple and the processing cost is relatively low. It has the advantage of being low cost. (Description of Preferred Embodiments of the Invention) As the oyster extract used in the treatment, oyster broth or a partial concentrate thereof is advantageously used. This raw persimmon extract liquid generally has a solid content concentration of 2 to 30% by weight, particularly 3 to 15% by weight. If the concentration exceeds the above range, the content of black to dark brown coloring components in the raw material extract will increase, which is undesirable, and if it is lower than the above range, it is economically disadvantageous because a large amount of liquid must be handled. As raw materials for oyster extract, in addition to those shown above, it is also possible to use extracts obtained by treating ground oyster meat under the action of heat and water. Of course, a desalted stock extract obtained by subjecting the stock extract to a desalting operation using an ion exchange membrane can also be used. As an example, Table 1 shows the ingredient list of dried oyster extract. Table 1 General ingredients Calories...354cal Water...2.6g Protein...38.1g Fat 0.2g Ash...9.2g Fiber...0g Carbohydrate (sugar) 49.9g Amino acid compositionEssential amino acids Isoleucine... 0.96g Leucine...1.56g Lysine...1.98g Methionine...0.63g Phenylalanine...0.86g Threonine...1.30g Tryptophan...0.22g Valine...1.24g Cysteine...0.36g Tyrosine...0.74g Arginine …1.82g Histidine …0.63g Alanine …1.85g Aspartic acid …2.98g Glutamic acid …4.25g Glycine …1.95g Proline …2.53g Serine …1.15g Inorganic calcium …115mg Phosphorus …552mg Manganese …2.28mg Magnesium 241mg Sodium 1860mg Potassium 1410mg Cobalt 14μg Iron …5.30mg Copper …1.9mg Zinc …40.2mg Iodine …0.6mg Vitamins Vitamin B 2 …1.67mg Vitamin B 6 …0.43mg Vitamin B 12 ...34μg Vitamin H (biotin)...27μg Inositol...93mg Choline 280mg Useful ingredient taurine...4.2g Glycogen...27g Phospholipid...10mg In the present invention, the specific surface area is 50m 2 /g or more, In particular, an adsorbent based on a water-insoluble inorganic magnesium compound in the range of 100 to 800 m 2 /g is used. A compound having a specific surface area smaller than the above range has an inferior ability to adsorb the precursor of the coloring component compared to that of the present invention. It is also important that this inorganic magnesium compound is substantially insoluble in water; water-soluble ones are undesirable in terms of the flavor of the concentrate. Inorganic magnesium compounds that are water-insoluble and have high adsorption performance used in the present invention include magnesium silicates, carbonates, partial acid adducts, partial hydroxides, etc., which are low in crystallinity and have a high specific surface area. is preferred. In particular, silicic acid and magnesium oxides and/or
Or obtained by hydrothermally treating hydroxide, with the following formula MgO・mSiO 2・nH 2 O However, it has a composition of 0.5≦m≦2, n≦2, and a ratio of 100 m 2 /g or more Magnesium silicate having a surface area is more preferably used, and among them, magnesium silicate with m=4/3 in the above composition formula is most preferable. The above composition (m=
4/3) Magnesium silicate is also represented by the following structural formula [Mg 3 ] (Si 2 O 5 ) 2 (OH) 2 ·xH 2 O (x≦5), and has a lattice spacing of 4.5 to 4.6. Å, 2.5~
It is a water-insoluble mineral substance composed of layered magnesium phyllosilicate having x-ray diffraction peaks at 2.6 Å and 1.5 to 1.6 Å and a specific surface area of 300 m 2 /g or more. The layered phyllosilicate mineral is synthesized by using synthetic silicic acid, natural diatomaceous earth, amorphous silica such as ferrosilicon dust, fired diatomaceous earth, crystalline silica such as silica stone, clay mineral, etc. as a silicic acid raw material. Active silicic acid or active aluminosilicic acid obtained by acid treatment, or a compound capable of forming silica under reaction conditions, is used, and as a magnesium raw material, magnesium oxide, hydroxide, or the above oxide under reaction conditions is used. This is achieved by using a compound capable of forming a hydroxide, mixing the two in an aqueous medium to form a slurry, and subjecting the slurry to a hydrothermal treatment under normal pressure or increased pressure. The reaction conditions used are temperatures between 80 and 200°C;
The pressure of the reaction system is maintained at 0.5 to 16 Kg/ cm2 , and the reaction time varies depending on the temperature and pressure, but the reaction time is 0.5 to 16 kg/cm2.
A range of 10 to 10 hours is appropriate. The product can be washed with water, if necessary, and subjected to post-treatments such as drying, pulverization, and classification to produce a water-insoluble white powder adsorbent. The synthetic layered magnesium phyllosilicate thus obtained is a natural clay mineral, as can be deduced from the above structural formula [Mg 3 ](Si 2 O 5 ) 2 (OH) 2 ·xH 2 O (x≦5). A structure similar to certain talc, namely MgO 6
It mainly has a three-layer structure in which two SiO 4 tetrahedral layers (phyllosilicic acid layers) are sandwiched together with an octahedral layer (brucite layer) in between, and the x-ray diffraction characteristic of this layered structure is unique to this layered structure. Has a spectrum. Figure 1 is an x-ray diffraction diagram of synthetic layered magnesium phyllosilicate most preferably used in the present invention, with interplanar spacings of 4.5 to 4.6 Å (corresponding to [0.20] and [110] planes), 2.5 to 2.6 Å ( [200] surface), and 1.5~
It is clear that each has a diffraction peak at 1.6 Å (corresponding to the [060] plane), which is an x-ray diffraction peak common to natural trioctahedral layered clay minerals. The synthetic layered magnesium phyllosilicate used in the present invention has an extremely large specific surface area and adsorption power that were not found in natural phyllosilicates such as talc. This is because synthetic layered magnesium phyllosilicate has low crystallinity, as seen from the broad shape of the x-ray diffraction peak, and the crystallites are fine and the layer stacking is irregular. This is probably because the structure allows other substances to easily enter between these layers. The adsorbent mainly composed of an inorganic magnesium compound used in the present invention may be used in powder form, but
In order to facilitate solid-liquid separation after adsorption treatment, adsorbent powder is molded in advance with water and, if necessary, water-insoluble cohesive minerals such as acid clay, white china clay (kaolin), or bentonite, and dried or It can also be solidified by calcination and used as a granular molded body. The inorganic magnesium compound is preferably added in an amount of 0.5 to 20% by weight, particularly 1 to 15% by weight, based on the persimmon extract. If it is lower than the above range, the removal of coloring substance precursors will be insufficient, and if it is higher than the above range, a substantial amount of umami components and nutritional components will be adsorbed and removed, which is not preferable for the purpose of the present invention. . In the present invention, in addition to using the above inorganic magnesium compound alone as an adsorbent, it can also be used in combination with other adsorbents such as activated clay, acid clay, silica, alumina, silica alumina, zeolite, and activated carbon. . The present inventors have discovered that when an inorganic magnesium compound and activated carbon are used in combination, precursors of coloring components can be most effectively adsorbed and removed without significantly reducing the content of umami components, etc. When an inorganic magnesium compound is used alone, it must be used in a fairly large amount in order to completely remove the precursor of the coloring component, and as a result, a considerable amount of umami components and the like will be adsorbed. Activated carbon is quite effective in removing precursors of coloring components, but its fatal drawback is that it simultaneously adsorbs umami components and the like, significantly reducing their content. When these two are used in combination, it becomes possible to effectively remove precursors of coloring components without significantly reducing umami components and the like. In this case, the inorganic magnesium compound is preferably used in an amount of 0.5 to 20% by weight, particularly 1 to 15% by weight, and the activated carbon is preferably used in an amount of 0.1 to 5% by weight, particularly 0.2 to 3% by weight, and the weight ratio of the two is preferably 2:1 to 10: It is best to set it to 1. It is best to contact the raw oyster extract with the inorganic magnesium compound and the activated carbon at the same time, but it is also possible to contact the raw oyster extract first with the activated carbon and then with the magnesium compound, or in the reverse order. The contact conditions between the raw oyster extract and the adsorbent are not particularly limited as long as the above-mentioned components are adsorbed and removed, but it is generally best to contact them at a temperature of 0 to 100°C for 1 minute or more, and at room temperature. Treatment with is particularly advantageous. For the adsorption treatment, any known adsorption purification method can be applied, such as adding adsorbent powder to the oyster extract and stirring for a predetermined period of time, followed by filtration separation, or passing the oyster extract through a tower filled with an adsorbent for adsorption treatment. can. The purified liquid after the adsorption treatment is concentrated in a substantially non-oxidizing atmosphere to a solid content concentration of 5% by weight or more. During concentration, it is desirable to effectively evaporate water at as low a temperature as possible, and for this reason, reduced pressure or vacuum concentration is desirable. Of course, azeotropic distillation using a solvent is also possible. Evaporative concentration using an inert gas such as nitrogen as a carrier gas is also possible. A multistage concentrator can also be used for efficient concentration. It can be made into a product in the form of a viscous liquid or paste as a concentrate, or it can be made into a product such as a powder granule by applying a drying method such as freeze drying or spray drying. It can also be made into plate-, flake-, or cake-like molded products by utilizing its own caking property or by using other food-quality binders, such as polysaccharides. According to the present invention, it is a decolorized concentrate of oyster extract, which contains amino acids, proteins, sugars, and various minerals as essential components, has a solid content of 5% by weight or more, and has the following formula: S=∫ 800 400 ε (x)dx In the formula, ε(x) is the wavelength x when measured using a cell with a thickness of 10〓 for a solution with a solid content concentration of 5% by weight.
It represents the absorbance in nanometers. Provided is a decolorized persimmon extract concentrate characterized by having an absorbance integral value S defined as 200 or less. The absorbance integral value S mentioned above is in the visible wavelength range from 400 to
It refers to the optical cumulative amount of all substances that have absorption in the 800 nanometer range, and is a numerical value that is inversely related to the transparency of the liquid. Conventional oyster extract concentrates generally have an integrated absorbance value S of 400 or more, and even partial concentrates generally show an integrated absorbance value of 250 or more, whereas the purified liquid according to the present invention has an integrated absorbance value S of 200 or less. Even when concentrated to a solid content of 40% by weight or more, it only shows an integrated absorbance value of 150 or less. FIG. 2 shows the visible region absorption spectra of the raw material extract and the concentrate obtained by the conventional method, and FIG. 3 shows the visible region absorption spectrum of the purified persimmon extract and its concentrate according to the present invention. From these comparisons, it can be seen that in the concentrate according to the present invention, the content of components having absorption on the short wavelength side is significantly reduced, and its increase due to concentration is also significantly suppressed. The concentrate according to the present invention is characterized by the removal of coloring components and the removal of off-flavor and off-flavor components based on the coloring components, but the umami and flavor components in the oyster extract are highly concentrated. Another notable feature is that it exists in form. The fact that the oyster extract concentrate according to the present invention has an elegant, mellow, and delicate umami and flavor cannot be confirmed without a sensory test as shown in the example below. The fact that it contains a high concentration of active ingredients other than those that are not present is clear by referring to its chromatogram. Figures 4 and 5 of the accompanying drawings show a purified solution of oyster extract stock solution treated using activated carbon alone so that the absorbance integral value was approximately 70 (Figure 4), and a purified solution treated with activated carbon alone to obtain an absorbance integral value of approximately 70. For the purified liquid (Figure 5) treated using the combination so that the absorbance integral value becomes the same value as above, the solid content concentration is 5.
A chromatogram obtained by high performance liquid chromatography using water as a developing solution and Gel G2500PWXL manufactured by Toyo Soda Kogyo Co., Ltd. as a column is shown. These comparisons reveal the fact that the concentrate according to the invention retains a higher concentration of the active ingredients in the persimmon extract. In the chromatogram shown in Figure 5, peak E is a peak specific to leucine and/or isoleucine, peak F is a peak specific to glutamic acid and/or succinic acid, and peaks G and H are peaks specific to leucine and/or isoleucine, and peaks G and H are peaks specific to glutamic acid and/or succinic acid. It should be noted that these peaks are significantly higher than those in the case of FIG. 4. In addition to the oyster extract obtained by this method, the present invention further provides bonito, mackerel, sea bream,
Extracts from fish and shellfish such as horse mackerel, yellowtail, scallops, shrimp, and crabs, seaweeds such as kelp, vegetables such as chicken bones and Chinese cabbage, reptiles such as pit vipers, and tortoise shells such as stupa turtles. Moreover, by applying the method of the present invention to a composite extract obtained by mixing the above-mentioned extracts with the persimmon extract used in the present invention, a decolorizing concentrate can be similarly obtained. (Example) The present invention will be explained with the following example. The test method for each characteristic in this example is as follows. (1) Method for measuring specific surface area of adsorbent Automatic BET (specific surface area) measuring device (Carlo
Measured using Sorptomatic Series 1800 (manufactured by Erba). (2) Method for measuring solid content concentration of oyster extract Measure the insoluble matter and impurities in the sample oyster extract with No.5C
The mixture was separated by filtration using quantitative filter paper, and the filtrate was used as a test solution.
Approximately 1 g of the test liquid is taken into a glass weighing bottle (ag) with a known weight and having a diameter of approximately 4 cm, and its weight (bg) is precisely weighed. It is then placed in a constant temperature dryer adjusted to 105°C and dried for 5 hours until it has a constant weight. After cooling in a desiccator, its weight (cg) is accurately weighed. The solid content concentration (weight %) is calculated using the following formula. Solid content concentration (wt%) = (c-a)/(b-a) x
100 (3) Method for measuring oyster extract absorbance integral value (S) Insoluble matter and impurities were separated in advance, and a sample oyster extract with a known solid content concentration was diluted with distilled water to a solid content concentration of 5% by weight to prepare a test solution. Obtain the absorption spectrum of the sample solution between wavelengths of 400 nanometers and 800 nanometers using an automatic recording spectrophotometer (JASCO Corporation double beam double monochromator spectrophotometer UVIDEC650) under the following conditions. Standard (control optical path): Distilled water Spectral width: 2.00 nm Time constant: 0.4 seconds Wavelength scanning range: 800 to 400 nm Wavelength scale: 40 nm/cm 3 Measurement scale: 0.000 to 5.000 Absorbance Cell used: 10 m/m quartz cell Absorbance integral value (S) is expressed by the following formula: S=∫ 800 400 ε(x)dx In the formula, ε(x) is measured using a cell with a thickness of 10 mm for a solution with a solid content concentration of 5% by weight. It represents the absorbance at wavelength x nanometers, and the absorbance integral value (S) is calculated by measuring the integral region area of the absorption spectrum diagram. (4) Chromatogram measurement method using high-performance liquid chromatography Separate insoluble matter and impurities in advance, and dilute a sample oyster extract with a known solid content concentration with distilled water to a solid content concentration of 5% by weight to use as a test solution. The chromatogram of the sample solution is measured using a high performance liquid chromatography device (manufactured by Nippon Waters Limited) under the following conditions. Column: Hydroxyl group-containing cross-linked vinyl polymer gel (Gel (G2500 PWXL) manufactured by Toyo Soda Kogyo Co., Ltd.) Developing solution: Water Flow rate: 0.8 ml/min Injection volume: 10 μ Pressure: 300 to 350 PSI Temperature: 20°C Detector: UV (254nm 1.0AUFS) Recorder full scale: 10mV (5) Oyster extract flavor test method Sample oyster extract concentrate and oyster extract diluted to a solid content of 5% by weight were used as test solutions. Ten well-trained people evaluated the flavor of the test solution. Those involved in cooking were asked to evaluate on a 10-point scale, and the average score was expressed.Example 1 1200g of oyster broth (solid content 6.2% by weight) was placed in a stainless steel container, and a synthetic layered material having a specific surface area of 639m 2 /g was poured into a stainless steel container. 60 g of magnesium phyllosilicate (trade name Mizukanite, manufactured by Mizusawa Chemical Industry Co., Ltd.) was added and stirred at a temperature of 30°C for 30 minutes, and the mixture was filtered using No. 5C quantitative filter paper to obtain a pale yellow transparent oyster extract liquid ( 1st step).Next, 1000g of oyster extract liquid obtained in the 1st step was added to 2
The mixture was placed in an eggplant-shaped flask and concentrated under reduced pressure at a temperature of 90° C. using a rotary evaporator (Yamato Scientific Model RE46A) to obtain 140 g of a viscous amber-colored persimmon extract concentrate (second step). When the solid content concentration of this product was measured, it was 43% by weight. Also, add 5% by weight of this product using distilled water.
The absorbance integral value S calculated from the absorption spectrum of the product diluted to a concentration of It had extremely excellent commercial value as a concentrate. Example 2 1300 g of oyster broth (solid content 6.2% by weight) was placed in a stainless steel container, and 195 g of reagent magnesium silicate (manufactured by Wako Pure Chemical Industries, Ltd.) having a specific surface area of 184 m 2 /g was added.
and stirred for 30 minutes at a temperature of 30°C.
It was filtered using 5C quantitative filter paper to obtain a pale yellow transparent oyster extract liquid (first step). Next, add 1000g of oyster extract liquid obtained in the first step to 2
Using a rotary evaporator, concentrate at a temperature of 90°C under reduced pressure to 158
A persimmon extract concentrate having a viscous amber color of 1.5 g was obtained (second step). When the solid content of this product was measured, it was found to be 38% by weight. In addition, the absorbance integral value S, chromatogram comparison results, and flavor test results of this product are as shown in Table 2, and it has extremely excellent commercial value as a persimmon extract concentrate. Example 3 Synthetic layered magnesium phyllosilicate and activated carbon were mixed at a weight ratio of 3:1, a compounding reaction was performed in the presence of water, and post-treatments such as filtration, drying, and pulverization were performed to obtain a specific surface area of 540 m 2 A composite adsorbent powder having a weight of 1.5%/g was obtained. Next, oyster broth (solid content concentration 6.2% by weight) 1200
g was placed in a stainless steel container, 25 g of the obtained composite adsorbent powder was added, and the mixture was stirred at a temperature of 30°C for 30 minutes. The mixture was filtered using No. 5C quantitative filter paper to obtain a pale yellow transparent oyster extract liquid. (1st step). Next, add 1000g of oyster extract liquid obtained in the second step to 2
Concentrate at 90°C under reduced pressure using a rotary evaporator to obtain 133%
A persimmon extract concentrate having a viscous amber color of 1.5 g was obtained (second step). When the solid content concentration of this product was measured, it was found to be 45% by weight. In addition, the absorbance integral value S, chromatogram comparison results, and flavor test results of this product are as shown in Table 2, and it has extremely excellent commercial value as a persimmon extract concentrate. Example 4 1,200 g of oyster broth (solid content 6.2% by weight) was placed in a stainless steel container, and 18 g of synthetic layered magnesium phyllosilicate (Mizukanite, manufactured by Mizusawa Chemical Industries, Ltd.) having a specific surface area of 639 m 2 /g and activated carbon (high-strength magnesium, manufactured by Takeda Pharmaceutical Co., Ltd.) were added. After adding 6 g of oyster extract (White Heron) and stirring at 30°C for 30 minutes, the mixture was filtered using No. 5C quantitative filter paper to obtain a pale yellow transparent oyster extract liquid (first step). Next, add 1000g of oyster extract liquid obtained in the first step to 2
Using a rotary evaporator, concentrate at a temperature of 90°C under reduced pressure to 154
A persimmon extract concentrate having a viscous amber color of 1.5 g was obtained (second step). When the solid content of this product was measured, it was found to be 39% by weight. In addition, the absorbance integral value S, chromatogram comparison results, and flavor test results of this product are as shown in Table 2, and it has extremely excellent commercial value as a persimmon extract concentrate. Example 5 1200 g of oyster broth (solid content 6.2% by weight) was placed in a stainless steel container, 60 g of synthetic hydrotalcite with a specific surface area of 168 m 2 /g and 7.2 g of activated carbon (Carbo Rhine manufactured by Takeda Pharmaceutical Company Limited) were added, and the mixture was heated at 30°C. The mixture was stirred at temperature for 30 minutes and filtered using No. 5C quantitative filter paper to obtain a pale yellow transparent oyster extract liquid (first step). Next, add 1000g of oyster extract liquid obtained in the first step to 2
Concentrate at a temperature of 90°C under reduced pressure using a rotary evaporator to obtain 143
A persimmon extract concentrate having a viscous amber color of 1.5 g was obtained (second step). When the solid content of this product was measured, it was found to be 42% by weight. In addition, the absorbance integral value S, chromatogram comparison results, and flavor test results of this product are as shown in Table 2, and it has extremely excellent commercial value as a persimmon extract concentrate. Example 6 Oyster extract concentrate obtained in the second step of Example 3
100 g was placed in a glass dish with a diameter of 30 cm, placed in a constant temperature dryer adjusted to 105°C, and dried for 8 hours to obtain a solid oyster extract. This solid product was ground in a tabletop sample mill to obtain an amber-colored persimmon extract powder. The absorbance integral value S calculated from the absorption spectrum of this persimmon extract powder dissolved in distilled water to a concentration of 5% by weight, the chromatogram comparison results, and the flavor test results are as shown in Table 2. It was an extremely excellent oyster extract powder. Example 7 1200g of oyster broth (solid content 6.2% by weight)
18 g of synthetic layered magnesium phyllosilicate (Mizunite, manufactured by Mizusawa Chemical Industry Co., Ltd.) with a specific surface area of 639 m 2 /g and 6 g of activated carbon (Shirasagi, manufactured by Takeda Pharmaceutical Co., Ltd.) were added to a eggplant-shaped flask, and the pressure was reduced using a rotary evaporator. It was concentrated at a temperature of 90° C. to obtain 211 g of viscous oyster extract concentrate containing adsorbent (first step). Next, the adsorbent was separated and removed from the oyster extract concentrate obtained in the first step using a small centrifuge (5000G) to obtain 165 g of a viscous amber-colored oyster extract concentrate (second step). When the solid content concentration of this product was measured, it was 41% by weight. In addition, the absorbance integral value S, chromatogram comparison results, and flavor test results of this product are as shown in Table 2, and it has extremely excellent commercial value as a persimmon extract concentrate. Example 8 1200g of oyster broth (solid content 6.2% by weight)
into an eggplant-shaped flask, and using a rotary evaporator, concentrate under reduced pressure at a temperature of 80°C to obtain 300 g.
An opaque brown oyster extract partial concentrate was obtained (first step). Next, add 639 g to 300 g of the partial concentrate obtained in the first step.
Synthetic layered magnesium phyllosilicate (Mizukanite manufactured by Mizusawa Chemical Industry Co., Ltd.) with a specific surface area of m 2 /g 18
Immediately after returning the vacuum pressure of the evaporator to normal pressure, add 6 g of activated carbon (Shirasagi made by Takeda Pharmaceutical Co., Ltd.) and stir at a temperature of 30°C for 60 minutes.
The adsorbent was separated and removed using a small centrifuge (5000G) to obtain 260 g of oyster extract partial concentrate having an amber color and a solid content concentration of 25% by weight (second step). Next, 250 g of the purified partially concentrated oyster extract liquid obtained in the second step was placed in an eggplant-shaped flask (1), and concentrated using a rotary evaporator at a temperature of 90°C under reduced pressure to obtain 152 g of concentrated oyster extract with a viscous amber color. A product was obtained (third step). When the solid content concentration of this product was measured, it was 41% by weight. In addition, the absorbance integral value S, chromatogram comparison results, and flavor test results of this product are as shown in Table 2, and it has extremely excellent commercial value as a persimmon extract concentrate. Comparative Example 1 Oyster broth (solid content 6.2% by weight) was filtered using No. 5C quantitative filter paper without adding any adsorbent.
A persimmon extract stock solution from which insoluble matter and impurities were removed was obtained (first step). Next, add 1000g of oyster extract liquid obtained in the first step to 2
Concentrate at 90°C under reduced pressure using a rotary evaporator to obtain 144%
g of a viscous black-brown oyster extract concentrate was obtained (second step). When the solid content concentration of this product was measured, it was 43% by weight. In addition, the absorbance integral value S, chromatogram comparison results, and flavor test results of this product are as shown in Table 2, and the product had a strong black coloring, had an off-taste and an off-odor, and lacked flavor. Comparative Example 2 1,200 g of oyster broth (solid content 6.2% by weight) was placed in a stainless steel container, 6 g of activated carbon (Takashi Shirasagi manufactured by Takeda Pharmaceutical Co., Ltd.) was added, and the mixture was stirred at a temperature of 30°C for 30 minutes. The activated carbon that leaked through the filtration was separated using a centrifuge (5000G) to obtain a transparent oyster extract liquid that was slightly blackish and pale yellow (first step). Next, add 1000g of oyster extract liquid obtained in the first step to 2
into an eggplant-shaped flask, and concentrated using a rotary evaporator at a temperature of 90°C under reduced pressure to obtain 150 g.
An oyster extract concentrate having a viscous blackish brown color was obtained (second step). When the solid content concentration of this product was measured, it was found to be 40% by weight. In addition, the absorbance integral value S, chromatogram comparison results, and flavor test results of this product are as shown in Table 2, and it was strongly colored, somewhat lacking in flavor, and inferior in commercial value. Comparative Example 3 1200 g of oyster broth (solid content 6.2% by weight) was placed in a stainless steel container, 15 g of activated carbon (Takashi Shirasagi, manufactured by Takeda Pharmaceutical Co., Ltd.) was added, and the mixture was stirred at a temperature of 30°C for 30 minutes. The mixture was filtered using a centrifugal separator (5000G) to separate activated carbon leaking through the filtration to obtain a transparent oyster extract liquid with a slight yellowish tinge (first step). Next, add 1000g of oyster extract liquid obtained in the first step to 2
Using a rotary evaporator, concentrate at a temperature of 90°C under reduced pressure to 158
A persimmon extract concentrate having a viscous amber color of 1.5 g was obtained (second step). When the solid content concentration of this product was measured, it was found to be 38% by weight. In addition, the absorbance integral value S, chromatogram comparison results, and flavor test results of this product are as shown in Table 2, and although there was little coloring, it lacked umami and flavor. Comparative example 4 1200g of oyster broth (solid content 6.2% by weight)
Using a rotary evaporator, concentrate at a temperature of 90°C under reduced pressure to obtain 230 g.
An oyster extract concentrate having a viscous blackish brown color and a solid content concentration of 35% by weight was obtained (first step). Next, 200g of oyster extract concentrate obtained in the first step
was placed in a stainless steel container, 19 g of synthetic layered magnesium phyllosilicate (Mizunite, manufactured by Mizusawa Chemical Industry Co., Ltd.) having a specific surface area of 639 m 2 /g and 19 g of activated carbon (Shirasagi, manufactured by Takeda Pharmaceutical Co., Ltd.) were added, and the mixture was heated at a temperature of 20°C for 30 minutes.
Stir for a minute and then use a small centrifuge (5000G)
The adsorbent was separated and removed to obtain a dark brown oyster extract concentrate (second step). When the solid content concentration of this product was measured, it was found to be 31% by weight. The absorbance integral value S, chromatogram comparison results, and flavor test results of this product are as shown in Table 2, and it was found to have a strong black coloration, an off-taste and an off-odor, and lacked flavor. Comparative Example 5 100 g of commercially available concentrated oyster extract (oyster sauce from Hong Kong) was diluted with 100 g of distilled water to obtain a diluted solution with a solid content concentration of 21% by weight. This diluted solution was separated from insoluble matter and impurities using a centrifuge (5000G) to obtain a brown, transparent oyster sauce solution with a solid content of 16% by weight. Furthermore, the residue after centrifugation was a large amount of pasty starch. The absorbance integral value S calculated from the absorption spectrum of the diluted and centrifuged oyster extract liquid diluted with distilled water to a concentration of 5% by weight, the chromatogram comparison results, and the flavor test results are as shown in Table 2. Yes, it is strongly colored as an oyster extract liquid,
The flavor was also a little bland.
【表】【table】
第1図は本発明実施例に用いた合成層状フイロ
ケイ酸マグネシウムのCu−Kα線によるX−線回
折スペクトルである。第2図は本発明実施例に用
いた原料カキエキスの可視部吸収スペクトルA、
比較例1による濃縮カキエキスの可視部吸収スペ
クトルBである。第3図は本発明実施例3の第1
工程にて得た精製カキエキスの可視部吸収スペク
トルC、実施例3の第2工程にて得た濃縮カキエ
キスの可視部吸収スペクトルDである。第4図は
比較例3の第1工程による精製カキエキスの水を
展開液とした高速液体クロマトグラフイーによる
クロマトグラムである。第5図は本発明実施例3
の第1工程による精製カキエキスの水を展開液と
した高速液体クロマトグラフイーによるクロマト
グラムである。
FIG. 1 is an X-ray diffraction spectrum of the synthetic layered magnesium phyllosilicate used in the Examples of the present invention using Cu-Kα rays. Figure 2 shows the visible absorption spectrum A of the raw material oyster extract used in the examples of the present invention.
1 is a visible absorption spectrum B of concentrated oyster extract according to Comparative Example 1. Figure 3 shows the first example of Embodiment 3 of the present invention.
These are the visible absorption spectrum C of the purified oyster extract obtained in the step, and the visible absorption spectrum D of the concentrated oyster extract obtained in the second step of Example 3. FIG. 4 is a chromatogram of the purified oyster extract obtained in the first step of Comparative Example 3 by high performance liquid chromatography using water as a developing solution. Figure 5 shows Example 3 of the present invention.
This is a chromatogram obtained by high performance liquid chromatography using water as a developing solution of the purified oyster extract obtained in the first step.
Claims (1)
に、比表面積が50m2/g以上の水不溶性無機マグ
ネシウム化合物を主体とする吸着剤を作用させて
吸着精製処理を行い、次いで精製液を実質上非酸
化雰囲気中で固形分濃度が5重量%以上となるよ
うに濃縮することを特徴とするカキエキス濃縮物
の製法。 2 無機マグネシウム化合物をカキエキス当り
0.5乃至20重量%の量で添加する特許請求の範囲
第1項記載の方法。 3 無機マグネシウム化合物が層状フイロケイ酸
マグネシウム塩である特許請求の範囲第1項記載
の方法。 4 吸着剤が無機マグネシウム化合物と活性炭と
の組合から成る特許請求の範囲第1項記載の方
法。 5 無機マグネシウム化合物を0.5乃至20重量%
及び活性炭を0.1乃至5重量%添加する特許請求
の範囲第4項記載の方法。 6 無機マグネシウム化合物及び活性炭を同時に
添加する特許請求の範囲第4項記載の方法。 7 無機マグネシウム化合物及び活性炭をこの順
序又は逆の順序に添加する特許請求の範囲第4項
記載の方法。 8 吸着精製処理を0乃至100℃の温度で1分間
以上行なう特許請求の範囲第1項記載の方法。 9 濃縮物が粘性液体である特許請求の範囲第1
項記載の方法。 10 濃縮物が粉末、顆粒、成形体である特許請
求の範囲第1項記載の方法。 11 カキエキスの脱色濃縮物であつて、必須成
分としてアミノ酸、たんぱく質、糖類及び各種ミ
ネラル分を含有し、5重量%以上の固形分を含有
し、且つ下記式 S=∫800 400ε(x)dx 式中ε(x)は固形分濃度5重量%の溶液につい
て、厚さ10m/mのセルを用いて測定した時の波
長xナノメータに於ける吸光度を表わす、 で定義される吸光度積分値Sが200以下であるこ
とを特徴とするカキエキス脱色濃縮物。 12 水を展開液及び水酸基含有架橋ビニル重合
体ゲル(東洋曹達工業株式会社製ゲル
G2500PWXL)をカラムとして使用した高速液体
クロマトグラフイーに於いて第5図に示すクロマ
トグラムと実質上同一のクロマトグラムを有する
特許請求の範囲第11項記載のカキエキス脱色濃
縮物。[Claims] 1. An adsorbent mainly composed of a water-insoluble inorganic magnesium compound having a specific surface area of 50 m 2 /g or more is applied to an oyster extract liquid having a solid content concentration of 30% by weight or less to perform an adsorption purification treatment, A method for producing a oyster extract concentrate, which comprises then concentrating the purified liquid in a substantially non-oxidizing atmosphere to a solid content concentration of 5% by weight or more. 2 Inorganic magnesium compound per oyster extract
2. The method according to claim 1, wherein the amount is between 0.5 and 20% by weight. 3. The method according to claim 1, wherein the inorganic magnesium compound is a layered magnesium phyllosilicate salt. 4. The method according to claim 1, wherein the adsorbent comprises a combination of an inorganic magnesium compound and activated carbon. 5 0.5 to 20% by weight of inorganic magnesium compound
and activated carbon in an amount of 0.1 to 5% by weight. 6. The method according to claim 4, wherein the inorganic magnesium compound and activated carbon are added at the same time. 7. The method according to claim 4, wherein the inorganic magnesium compound and activated carbon are added in this order or in the reverse order. 8. The method according to claim 1, wherein the adsorption purification treatment is carried out at a temperature of 0 to 100°C for 1 minute or more. 9 Claim 1 in which the concentrate is a viscous liquid
The method described in section. 10. The method according to claim 1, wherein the concentrate is a powder, granules, or molded body. 11 A decolorized concentrate of oyster extract, which contains amino acids, proteins, sugars, and various minerals as essential components, and has a solid content of 5% by weight or more, and has the following formula: S=∫ 800 400 ε(x)dx In the formula, ε(x) represents the absorbance at wavelength x nanometer when measured using a cell with a thickness of 10 m/m for a solution with a solid content concentration of 5% by weight, and the absorbance integral value S defined as A decolorized oyster extract concentrate characterized by having a concentration of 200 or less. 12 Add water to the developing solution and hydroxyl group-containing crosslinked vinyl polymer gel (manufactured by Toyo Soda Kogyo Co., Ltd.)
12. The decolorized persimmon extract concentrate according to claim 11, which has a chromatogram that is substantially the same as the chromatogram shown in FIG. 5 in high performance liquid chromatography using G2500PWXL as a column.
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61006371A JPS62166866A (en) | 1986-01-17 | 1986-01-17 | Concentration of oyster essence and its concentrate |
| KR1019870000381A KR930000828B1 (en) | 1986-01-17 | 1987-01-17 | Process for the preparation of oyster extracts |
| EP87300400A EP0232035B1 (en) | 1986-01-17 | 1987-01-19 | Decolorized oyster extract concentration |
| ES87300400T ES2015571B3 (en) | 1986-01-17 | 1987-01-19 | CONCENTRATION OF DISCOLORED OYSTER EXTRACT. |
| US07/004,573 US4770894A (en) | 1986-01-17 | 1987-01-20 | Decolorized oyster extract concentrate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61006371A JPS62166866A (en) | 1986-01-17 | 1986-01-17 | Concentration of oyster essence and its concentrate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62166866A JPS62166866A (en) | 1987-07-23 |
| JPH0461630B2 true JPH0461630B2 (en) | 1992-10-01 |
Family
ID=11636508
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61006371A Granted JPS62166866A (en) | 1986-01-17 | 1986-01-17 | Concentration of oyster essence and its concentrate |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62166866A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4849643B2 (en) * | 2008-04-30 | 2012-01-11 | 株式会社渡辺オイスター研究所 | Extracting ingredients from oyster meat extract concentrate |
-
1986
- 1986-01-17 JP JP61006371A patent/JPS62166866A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62166866A (en) | 1987-07-23 |
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