JP3408919B2 - Method for producing purple sweet potato pigment - Google Patents
Method for producing purple sweet potato pigmentInfo
- Publication number
- JP3408919B2 JP3408919B2 JP07289896A JP7289896A JP3408919B2 JP 3408919 B2 JP3408919 B2 JP 3408919B2 JP 07289896 A JP07289896 A JP 07289896A JP 7289896 A JP7289896 A JP 7289896A JP 3408919 B2 JP3408919 B2 JP 3408919B2
- Authority
- JP
- Japan
- Prior art keywords
- sweet potato
- purple sweet
- pigment
- dried
- dye
- 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
Landscapes
- Coloring Foods And Improving Nutritive Qualities (AREA)
Description
【発明の詳細な説明】
【0001】
【産業上の利用分野】本発明は、耐光性、耐熱性に優れ
た安定な紫さつまいも色素を工業的に有利に製造するこ
とに関する。
【0002】
【従来の技術】赤キャベツ、ブドウ、紫トウモロコシ、
ベリー類、赤ダイコン、赤カブ等から製造される赤色天
然色素は、アントシアニン色素に属している。紫さつま
いもも同様なアントシアニン色素を含有した赤色色素原
料である。最近紫さつまいも色素は、他のアントシアニ
ン色素に比べ、耐熱性・耐光性、色調の鮮やかさに優れ
ていることから、食品への利用が増加してきている。
【0003】紫さつまいも色素の製造方法に関してはい
くつか提案されている。紫さつまいもを生あるいは蒸煮
したものを酸性条件下の水または含水エタノールで抽出
し、抽出物を精製処理を行うことにより、紫さつまいも
色素を製造する方法(特開昭62−297363、特開
昭62−297364)はその1例である。また、原料
である紫さつまいもを10℃以下にしたものから色素を
抽出する方法、同じく凍結粉砕した紫さつまいもから色
素を抽出する方法(特開平4−103669)は何れも
酵素の活性を抑制することを特徴とした紫さつまいも色
素を製造する方法である。しかしながらこれらの提案に
おける製造方法においては、色素の抽出効率の点で必ず
しも満足できるものではない。それは、原料である紫さ
つまいもの種類が、アントシアニン色素の含量の極めて
少ないブラジル原産紫さつまいも(Ipoea batas, Lam..
Convolvlaceae)、山川紫、種子島在来、頴娃紫、知覧
紫、喜入紫、ナカムラサキ、等に限定されているため、
これらを使用して色素を抽出する方法は工業的レベルで
の抽出効率が満足できるものではない。又、紫さつまい
もを低温で酸化酵素の作用を抑制する際、温度管理を厳
重にする必要があり、粉砕などにおける摩擦熱などの管
理が必要となる。
【0004】そこで、紫さつまいもの品種を改良しその
改良品種九州113号(登録名:甘しょ農林47号、通
称「アヤムラサキ」(以下、アヤムラサキと記す))を
色素原料とすることにより、紫さつまいも色素を高収率
で得る方法(特開平7−126544、特開平7−22
7246)を提案した。しかしながら、これら全ての提
案においては原料の紫さつまいもの収穫時に集中して製
造することが前提となっており、色素の製造する時期を
ずらすには、通常野菜の保管に用いる加湿冷蔵や冷凍保
存で保管することが必要となってくる。しかし、原料で
ある紫さつまいもを生のままで保管しようとすると、保
管場所(容積)が広く必要となり、又加湿冷蔵により腐
敗や紫さつまいも色素の分解が進行するため、短期間し
か保管することが出来なかった。
【0005】保管を長期間経済的に行う方法として、原
料の紫さつまいもを乾燥する方法が挙げられる。乾燥の
方法としては、熱風で乾燥する方法、天日に干して自然
乾燥する方法、紫さつまいもを蒸したものをドラム乾燥
する方法などが挙げられる。しかし、加熱することによ
り、紫さつまいも色素成分が分解したり、含有する澱粉
がα化したりするため、これらの方法で乾燥した紫さつ
まいもを原料として色素を製造しても、色調が黄みがか
ったり、また、製造工程の濾過の過程で目詰まりしたり
するなど、工業的に利用できるものではなかった。
【0006】また、凍結して乾燥する方法もあるが、乾
燥工程が複雑で高価な設備が必要となってくるため、経
済的負担という面でも工業的に有利に利用できるもので
はなかった。
【0007】
【発明が解決しようとする課題】本発明は、工業的に有
利に紫さつまいも色素を製造する方法を提供することを
目的とする。
【0008】
【発明を解決するための手段】本発明者らは、紫さつま
いもから工業的に有利に紫さつまいも色素を製造する方
法に際し、鋭意研究を重ねた結果、乾燥粉砕した紫さつ
まいも改良品種「アヤムラサキ」を用いて製造する本発
明に至った。紫さつまいもの乾燥技術を説明する。生の
紫さつまいもをスライサーにより角千切りにする。角千
切りの大きさとしては、厚さ約2〜5mm、幅約3〜6
mm、長さ約10〜100mmの大きさでよい。送風乾
燥を2段階に分け、直交式通風乾燥方式や回転通気式乾
燥方式の設備を用い、前段階は70〜80℃で15〜3
0分し、後段階は55〜65℃で1〜4時間乾燥する。
この乾燥方法によると、含有する水分量は10%以下に
なり、色素の分解を20%前後に押さえることが可能に
なる。
【0009】従来の技術である熱風乾燥や天日乾燥の色
素分解度を調べたところ、前者は50〜60%、後者は
60〜70%色素が分解した。しかも、本発明の直交式
通風乾燥方式や回転通気式乾燥方式で乾燥した乾燥物は
色調が鮮やかな赤色だったのと比較して、熱風乾燥や天
日乾燥を行った乾燥物は、色調が黄色っぽい褐色に変化
する。
【0010】乾燥された紫さつまいもは、そのままでも
良いが、粉砕機により粉末にした方がより好ましい。粉
砕の大きさは自由に調整でき、3.5〜200メッシュ
好ましくは20〜70メッシュに調整する。
【0011】すぐに色素の製造を行わない場合には、乾
燥した紫さつまいも乾燥粉砕物はそのまま、あるいは粉
砕粉末化した粉砕粉末品を酸素の通気性の少ないポリエ
チレン製、ポリ塩化ビニル製やアルミ包装容器等の包装
容器に入れて比較的温度の一定した倉庫などで長期保管
できる。 また、紫さつまいも乾燥粉砕物は生の紫さつ
まいもと比較して容積が非常に小さくなる。乾燥粉砕前
の生の紫さつまいもの容積を1とすると、乾燥粉砕後の
紫さつまいも乾燥粉砕物の容積は、粉砕の大きさにより
1/2〜1/5に減少する。
【0012】さらに、紫さつまいも乾燥粉砕物は、水分
含有量が10%以下となり、細菌やカビなどの増殖を抑
制できるので、生の紫さつまいもに比べて、長期間保管
可能となる。この方法で紫さつまいもを乾燥粉砕するこ
とによって、得られた紫さつまいも乾燥粉砕物を長期間
保管できるようになったので、色素の製造する時期を紫
さつまいもの収穫時に集中して行わなくてもよい。
【0013】次に、上記の紫さつまいも乾燥粉砕物を抽
出する溶媒として、酸性条件下の水または含水エタノー
ルを使用する。その抽出液のpH約5以下の酸性とし前
記乾燥粉砕物が浸漬できる量を用意する。このときのp
H5以下とするのは、アントシアニン色素がこれ以上で
あると不安定で退色するためである。このとき使用する
pH調整剤としては、クエン酸、酒石酸、リンゴ酸など
の有機酸、あるいは、塩酸、硫酸等の無機酸のいずれで
もよい。乾燥粉砕物と抽出液の割合は、例えば、乾燥粉
砕物1部に対して抽出液2〜20部好ましくは5〜10
部でよい。
【0014】また、系の温度は、室温でもよく澱粉がα
化(糊化)しない温度(64℃以下)で例えば、50〜
60℃で設定することで時間を短縮できるなど抽出効率
が良くなる。乾燥粉砕物に含まれているアントシアニン
色素は、抽出液に短時間で色素の全量が抽出液に移行す
る。アントシアニン色素の移行が終わった時点で抽出操
作を止め、残渣を取り除いてアントシアニン色素のみを
採取する。残渣の除去は、濾過、遠心分離等の固体と液
体を分離する手段を用いればよい。
【0015】例えば、生のさつまいも100kgを0.
5重量%硫酸水溶液1tで20℃で抽出し、プレス濾過
(1m×1m×10枚)を実施したときの仕込みから抽
出できるまでの時間を測定した。抽出で3時間、プレス
濾過ではさつまいもが目詰まりを起こしたため、1時間
要し、完了するまでに約5時間を要した。一方、紫さつ
まいも乾燥粉砕物を同様の条件で仕込んだ時、抽出の
際、乾燥粉砕物に含まれているアントシアニン色素は、
生のさつまいもを使用したときに比べて抽出液に短時間
で色素の全量が抽出液に移行したので1時間で終了し、
濾過も目詰まりを起こすことなく40分で終わり、抽出
から濾過の工程の完了まで、約2時間かかった。生の紫
さつまいもの使用時に比べて、乾燥粉砕物使用時は抽出
から濾過に要した時間を半分以下の時間に短縮できた。
【0016】濾過された抽出液はバッチ殺菌、またはプ
レート殺菌などの加熱処理を行うことで変色や菌の増殖
を防止することができる。これらの温度は、バッチ殺菌
で約80〜100℃、30〜60分間程度の加熱で充分
であり、プレート殺菌においては、約100〜120
℃、20秒〜30分程度の加熱で充分である。このよう
にして得られた色素液をそのまま使用してもよいし、あ
るいは濃縮して濃縮色素としてもよい。更には、噴霧乾
燥法等で粉末化することもできる。また、濃縮した紫さ
つまいも色素を乳化することもできる。乳化方法は通
常、アラビアガム、ショ糖脂肪酸エステル、グリセリン
脂肪酸エステル等の乳化剤を添加して乳化することによ
り行うことができる。
【0017】本発明により得られた紫さつまいも色素
は、食品、医薬品、化粧品等の着色に利用することがで
きる。食品としては、飲料、ゼリー、冷菓、アイスクリ
ーム、キャンディ、錠菓、チョコレート菓子、漬物等が
あげられる。医薬品としては、錠剤、湿布薬、液剤、化
粧品としては石鹸、洗剤、シャンプー、口紅などがあげ
られる。
【0018】
【実施例】以下、実施例を示し本発明をより詳しく説明
する。
【0019】実施例1
紫さつまいも「アヤムラサキ」5kgをスライサーによ
り厚さ3mm、幅2mm、長さ20mmに角千切りに
し、回転通風式乾燥機で70〜75℃で20分間、続い
て60℃で1時間乾燥した。得られた乾燥物を粉砕機を
用いて粉砕し、32メッシュの篩を通過させて紫さつま
いも乾燥粉砕物2kgを得た。得られた紫さつまいも乾
燥粉砕物の水分含有率は7.5%であった。この紫さつ
まいも乾燥粉砕物1kgを0.5重量%硫酸水溶液10
lの抽出液に投入し、18℃で60分間抽出し、抽出後
濾過して不溶性固形物を除き抽出液8.3kgを得た。
この液を、ダイアイオンHP−20(三菱化成工業株式
会社製吸着樹脂)500mlに吸着させてから、水洗し
たのち58容量%エチルアルコール500mlを用いて
その吸着されている色素を溶出した。得られた色素液を
真空濃縮機にて150gに濃縮後、95%エチルアルコ
ール15g、クエン酸1g、水34gを添加して、紫さ
つまいも色素液200gを得た。取得した紫さつまいも
色素は、鮮明な赤色を呈し、炭酸飲料に着色したとき、
室温に1カ月置いても何らの色調変化及び不溶解物を生
じなかった。
【0020】比較例1
紫さつまいも「アヤムラサキ」1kgを洗浄し、100
℃の蒸気で30分蒸し上げた後ドラムドライヤーで乾
燥、粉砕機にて粉砕し、32メッシュを通過した蒸し上
げ粉末品150gを得た。蒸し上げ粉末品と生の紫さつ
まいもをスライサーにより厚さ3mm、幅2mm、長さ
20mmに角千切りにしたものとを実施例1と同様の処
理を行い各々の色素を得た。クエン酸0.1重量%10
0g水溶液に実施例1の乾燥粉砕物から得た色素、蒸し
上げ粉末品から得た色素、及び生の紫さつまいもから得
た色素を各々(色価80換算)0.05g添加し、肉眼
により色調観察した。その結果を表1に示す。また、回
収した色素量から各々の原料の色価を計算した。
【0021】
【表1】
【0022】色価:色素の濃度(色力)を意味し、一般
に分光光度計にて測定され、測定値を10%濃度の値に
換算して表される。分光光度計の測定は、一般に、最大
吸収波長における吸光度を0.2〜0.7の範囲になる
ように色素の濃度を調製して行われる。例えば色素濃度
0.1容量/重量%にて、最大吸収波長における吸光度
(λmax O.D.)が0.5の場合10÷0.1=
100 色価=0.5×100=50と表す。
【0023】表1より、本発明に係る製法で作製した色
素は、生の紫さつまいもから作製した色素と同様の明る
い赤色の色調を示し、しかも、高い色素含有量を示し
た。それと比較して、蒸し上げ粉末品は明るい赤色色素
とはならなかった。蒸し上げ粉末品に関して色素含有量
が高い値を示したのは、熱による変化が認められ、色調
が黄色くなり黄色の成分も原料色価に含まれていたから
である。
【0024】比較例2
紫さつまいも「アヤムラサキ」5kgをスライサーによ
り厚さ3mm、幅2mm、長さ20mmに角千切りに
し、天日により5日間乾燥し、紫さつまいも天日乾燥品
2kgを得た。また、上記「アヤムラサキ」角千切り物
5kgを乾燥機を用いて80℃の熱風で3時間乾燥し、
紫さつまいも熱風乾燥品1.8kgを得た。天日乾燥
品、熱風乾燥品を色素原料として、実施例1の方法で色
素を製造し、色調を肉眼により観察した。その結果を表
2に記す。
【0025】
【表2】
【0026】表2より、本発明に係る製法で作製した色
素は明るい赤色となった。しかし、天日乾燥と熱風乾燥
を行った抽出原料から作製した色素は、乾燥によって色
調が変わったために明るい赤色とはならなかった。
【0027】比較例3
実施例1の紫さつまいも「アヤムラサキ」乾燥粉砕物を
32メッシュの篩で通過した粉砕粉末物70gと、粉砕
粉末品70gとほぼ同量の色素量をもつ生の紫さつまい
も「アヤムラサキ」1Kgを3〜5mm角千切りし、
0.5重量%硫酸水溶液10lの抽出液に投入し、20
℃で60分間色素の抽出を行った。時間と抽出された色
素量の関係を図1に示す。
【0028】図1より、本発明に係る製法では、生の紫
さつまいもを用いた製法より約6分の1の時間で抽出が
終了することが判った。
【0029】比較例4
実施例1の紫さつまいも「アヤムラサキ」乾燥粉砕物1
00gを0.5重量%硫酸水溶液1lの抽出液に投入
し、45℃10分間紫さつまいも抽出を行い抽出色素液
800gを得た。同様に比較例2の方法で蒸し上げた後
乾燥粉末にした蒸し上げ粉末品100g、及び生の紫さ
つまいも300gを同様に45℃10分間抽出し色素液
を得た。
【0030】これら抽出液をΦ9cmの吸引濾過器で濾
紙濾過(ADVANTEC FILTER PAPER
5C)を行い抽出液の濾過開始から濾過終了までの時
間を測定し表3に示した。
【0031】
【表3】
【0032】表3より、本発明に係る製法では、蒸し上
げ粉末や生の紫さつまいもを使用した製法と比べて、濾
過に要した時間が短縮された。
【0033】比較例3、4から明らかなように、本発明
に係る製法では、他の製法と比較して製造に要する時間
を大幅に短縮することが出来、工業的有利に製造できる
ことが判った。
【0034】比較例5
実施例1の紫さつまいも「アヤムラサキ」乾燥粉砕物と
紫さつまいも「アヤムラサキ」の蒸し上げた後ドラムド
ライヤーで乾燥した粉砕粉末品を15℃以下の倉庫に保
管、及び生の紫さつまいもを15℃、過飽和状態の加湿
冷蔵庫に保管したときの含有色素の残存率(%)と肉眼
による腐敗の関係を調べ表4に示した。
【0035】
【表4】【0036】表4より、本発明に係る製法で作製した色
素は、生のさつまいもを用いた製法で作製した色素に比
べての色素の品質の低下がほとんどなく、長期保管が可
能であることが判る。
【0037】実施例2
実施例1の紫さつまいも「アヤムラサキ」の乾燥粉砕物
1kgを0.01重量%硫酸添加50容量%アルコール
水溶液10lの抽出液に投入し、25℃60分間抽出
し、濾過して不溶性固形物を除き抽出液8.5kgを得
た。この液を5lまで濃縮し、ダイアイオンHP−20
(三菱化成工業株式会社製吸着樹脂)500mlに吸着
させてから、水洗したのち58容量%エチルアルコール
500mlを用いてその吸着されている色素を溶出し
た。得られた色素液を真空濃縮機にて80gに濃縮、グ
リセリン脂肪酸エステル3g、ショ糖脂肪酸エステル2
g、食用油16g、アラビアガム40g、95%エチル
アルコール20g、クエン酸10g、グリセリン20
g、水9gを添加してホモディスパーにて攪拌混合し紫
さつまいも2重乳化色素液200gを得た。取得した紫
さつまいも色素は、ゼリーに着色しシロップ漬けにした
とき鮮明な赤色を呈し、室温に1カ月置いても何らの色
調変化及びシロップ部への色流れを生じなかった。
【0038】
【発明の効果】本発明により、従来の紫さつまいも色素
の製造法に比較して、製造に要する時間が大幅に短縮が
出来、色素の変色退色に関与していた酸化酵素による妨
害もなくなる。しかも、紫さつまいもを乾燥粉砕物にす
ることで長期保管することが出来るので、集中して色素
の製造を行う必要がなくなり、色調に優れた紫さつまい
も色素を効率よく、工業的に有利に製造することが出来
る。
【0039】Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an industrially advantageous production of a stable purple sweet potato dye excellent in light resistance and heat resistance. [0002] Red cabbage, grapes, purple corn,
Red natural pigments produced from berries, red radish, red turnip and the like belong to anthocyanin pigments. Purple sweet potato is also a red pigment raw material containing a similar anthocyanin pigment. In recent years, purple sweet potato dyes have been increasingly used in foods because they are more excellent in heat resistance, light resistance and vividness of color tone than other anthocyanin dyes. Several methods have been proposed for producing purple sweet potato dyes. A method for producing a purple sweet potato pigment by extracting a raw or steamed purple sweet potato with water or aqueous ethanol under acidic conditions and subjecting the extract to a purification treatment (Japanese Patent Application Laid-Open Nos. 62-297363 and 62 -297364) is one such example. In addition, the method of extracting a dye from a purple sweet potato as a raw material at a temperature of 10 ° C. or less, and a method of extracting a dye from a frozen and sweetened purple sweet potato (Japanese Patent Application Laid-Open No. 4-103669) all inhibit the activity of the enzyme. This is a method for producing a purple sweet potato pigment characterized by the following. However, the production methods in these proposals are not always satisfactory in terms of dye extraction efficiency. The kind of purple sweet potato that is the raw material is Brazilian purple sweet potato with a very low content of anthocyanin pigment (Ipoea batas, Lam ..
Convolvlaceae), purple from Yamakawa, native to Tanegashima, ei purple, Chiran purple, Kiire purple, Nakamurasaki, etc.
The method of extracting a pigment by using them does not have satisfactory extraction efficiency on an industrial level. In addition, when suppressing the action of oxidase at low temperature on purple sweet potato, it is necessary to strictly control the temperature, and it is necessary to control frictional heat in grinding and the like. Therefore, the purple sweet potato variety is improved and the improved variety Kyushu No. 113 (registered name: Asho Norin 47, commonly known as "Ayamurasaki" (hereinafter referred to as "Ayamurasaki")) is used as a pigment raw material. Methods for obtaining dyes in high yield (JP-A-7-126544, JP-A-7-22
7246). However, in all of these proposals, it is premised that the raw material of purple sweet potatoes is produced at the time of harvesting, and in order to stagger the time of production of the pigment, humidification refrigeration or frozen storage usually used for storage of vegetables is used. It becomes necessary to keep it. However, if raw purple sweet potatoes are stored raw, a large storage space (volume) is required, and the decomposition of rot and purple sweet potatoes due to humidification and refrigeration progresses. I could not do it. [0005] As a method of economically storing for a long period of time, there is a method of drying a purple sweet potato as a raw material. Examples of the drying method include a method of drying with hot air, a method of drying on the sun and natural drying, and a method of drum-drying steamed purple sweet potato. However, due to the heating, the purple sweet potato also decomposes the pigment component, or the starch contained therein becomes alpha, so even if the pigment is produced using the dried purple sweet potato as a raw material by these methods, the color tone becomes yellowish. In addition, they are not industrially usable, such as clogging during the filtration process in the production process. There is also a method of drying by freezing, but since the drying step is complicated and expensive equipment is required, it cannot be used industrially advantageously in terms of economic burden. SUMMARY OF THE INVENTION It is an object of the present invention to provide a method for producing purple sweet potato pigment which is industrially advantageous. Means for Solving the Problems The present inventors have conducted intensive studies on a method for producing purple sweet potato pigment from purple sweet potato in an industrially advantageous manner. The present invention, which is manufactured using Ayamurasaki, has been achieved. The drying technique of purple sweet potato will be described. Cut the raw purple sweet potatoes into slices with a slicer. As for the size of the square cut, the thickness is about 2 to 5 mm and the width is about 3 to 6
mm and a length of about 10 to 100 mm. Blast drying is divided into two stages, using orthogonal ventilation drying system or rotary ventilation drying system equipment, the former stage is performed at 70-80 ° C and 15-3.
After 0 minutes, the subsequent step is dried at 55-65 ° C. for 1-4 hours.
According to this drying method, the water content is 10% or less, and the decomposition of the dye can be suppressed to about 20%. Examination of the degree of pigment decomposition in hot air drying and sun drying, which are conventional techniques, revealed that the pigment was decomposed in the former by 50 to 60% and in the latter by 60 to 70%. Moreover, compared to the dried product dried by the orthogonal ventilation drying method or the rotary ventilation drying method of the present invention, the color tone of the dried product subjected to hot-air drying or solar drying is lower than that of the dried product having a bright red color. Turns yellowish brown. Although the dried purple sweet potato may be used as it is, it is more preferable to make it into a powder with a pulverizer. The size of the pulverization can be freely adjusted, and is adjusted to 3.5 to 200 mesh, preferably 20 to 70 mesh. In the case where the pigment is not immediately produced, the dried purple sweet potato is dried or pulverized as it is, or the pulverized powder obtained by pulverizing and pulverizing is made of polyethylene, polyvinyl chloride, aluminum packaging or the like having a low oxygen permeability. It can be stored for a long time in a container with a relatively constant temperature by putting it in a packaging container such as a container. Also, the dried and ground purple sweet potato has a very small volume as compared with the raw purple sweet potato. Assuming that the volume of the raw purple sweet potato before the dry pulverization is 1, the volume of the dried and ground purple sweet potato after the dry pulverization is reduced to 1/2 to 1/5 depending on the size of the pulverization. Further, the dried and ground purple sweet potato has a water content of 10% or less and can suppress the growth of bacteria and fungi, so that it can be stored for a long time as compared with the raw purple sweet potato. By drying and pulverizing the purple sweet potato in this method, the resulting dried and dried purple sweet potato can be stored for a long period of time, so that the time of producing the pigment does not have to be concentrated on harvesting the purple sweet potato. . Next, as a solvent for extracting the dried and ground purple sweet potato, water or aqueous ethanol under acidic conditions is used. The extract is acidified to have a pH of about 5 or less, and an amount is prepared for immersing the dried and crushed product. P at this time
The reason for setting it to H5 or less is that if the anthocyanin dye is more than this, it will be unstable and fade. The pH adjuster used at this time may be any of organic acids such as citric acid, tartaric acid, malic acid, and inorganic acids such as hydrochloric acid and sulfuric acid. The ratio of the dry pulverized product to the extract is, for example, 2 to 20 parts of the extract, preferably 5 to 10 parts per 1 part of the dry pulverized product.
Department. The temperature of the system may be room temperature, and the starch may be α
At a temperature (64 ° C. or less) at which no gelatinization (gelatinization) occurs,
By setting the temperature at 60 ° C., the extraction efficiency is improved, for example, the time can be reduced. As for the anthocyanin pigment contained in the dried and ground product, the entire amount of the pigment is transferred to the extract in a short time in the extract. When the transfer of the anthocyanin dye is completed, the extraction operation is stopped, the residue is removed, and only the anthocyanin dye is collected. The residue may be removed by using a means for separating a solid and a liquid, such as filtration and centrifugation. [0015] For example, 100 kg of raw sweet potato is added to 0.1 kg.
Extraction was carried out at 20 ° C. with 1 ton of 5% by weight sulfuric acid aqueous solution, and the time from preparation to extraction when press filtration (1 m × 1 m × 10 sheets) was carried out was measured. Extraction took 3 hours, and press filtration took 1 hour due to clogging of the sweet potato, and took about 5 hours to complete. On the other hand, when purple sweet potatoes were prepared by drying and pulverized under the same conditions, during extraction, the anthocyanin dye contained in the dried and pulverized products was
Compared to when using raw sweet potatoes, the whole amount of pigment was transferred to the extract in a short time in the extract, so it finished in 1 hour,
Filtration was completed in 40 minutes without clogging, and it took about 2 hours from extraction to completion of the filtration process. Compared with the use of raw purple sweet potatoes, the time required for extraction to filtration was reduced to less than half when using the dried and ground product. The filtered extract is subjected to heat treatment such as batch sterilization or plate sterilization to prevent discoloration and proliferation of bacteria. These temperatures are sufficient to heat about 80 to 100 ° C. for about 30 to 60 minutes in batch sterilization, and about 100 to 120 in plate sterilization.
C. and heating for about 20 seconds to 30 minutes is sufficient. The dye solution thus obtained may be used as it is, or may be concentrated to a concentrated dye. Further, the powder can be made into a powder by a spray drying method or the like. In addition, concentrated purple sweet potato can also emulsify the pigment. The emulsification method can be usually carried out by adding an emulsifier such as gum arabic, sucrose fatty acid ester, glycerin fatty acid ester, and emulsifying. The purple sweet potato pigment obtained according to the present invention can be used for coloring foods, pharmaceuticals, cosmetics and the like. Foods include beverages, jellies, frozen desserts, ice creams, candy, tablets, chocolate confections, pickles, and the like. Pharmaceuticals include tablets, poultices, solutions, and cosmetics include soaps, detergents, shampoos, and lipsticks. The present invention will be described below in more detail with reference to examples. Example 1 5 kg of Ayamurasaki purple sweet potato was sliced into slices having a thickness of 3 mm, a width of 2 mm, and a length of 20 mm using a slicer, and a rotary ventilation dryer at 70 to 75 ° C. for 20 minutes, followed by 1 hour at 60 ° C. Dried for hours. The obtained dried product was pulverized using a pulverizer and passed through a 32-mesh sieve to obtain 2 kg of a dried and pulverized purple sweet potato. The water content of the dried and ground purple sweet potato obtained was 7.5%. 1 kg of the dried and ground purple sweet potato is added to a 0.5 wt% sulfuric acid aqueous solution 10
of the extract, extracted at 18 ° C. for 60 minutes, filtered after the extraction to remove insoluble solids, to obtain 8.3 kg of the extract.
This solution was adsorbed on 500 ml of Diaion HP-20 (adsorption resin manufactured by Mitsubishi Kasei Kogyo Co., Ltd.), washed with water, and the adsorbed dye was eluted with 500 ml of 58% by volume ethyl alcohol. The obtained dye solution was concentrated to 150 g with a vacuum concentrator, and then 15 g of 95% ethyl alcohol, 1 g of citric acid and 34 g of water were added to obtain 200 g of a purple sweet potato dye solution. The acquired purple sweet potato pigment presents a clear red color and when colored into carbonated beverages,
One month storage at room temperature did not produce any color change or insolubles. Comparative Example 1 1 kg of purple sweet potato "Ayamurasaki" was washed and 100
After steaming with steam at 30 ° C. for 30 minutes, the product was dried with a drum dryer and pulverized with a pulverizer to obtain 150 g of a steamed powder product having passed through a 32 mesh. The steamed powdered product and the raw purple sweet potato were sliced into slices having a thickness of 3 mm, a width of 2 mm, and a length of 20 mm using a slicer, and the same treatment as in Example 1 was carried out to obtain respective pigments. Citric acid 0.1% by weight 10
To a 0 g aqueous solution, 0.05 g of each of the pigment obtained from the dried and ground product of Example 1, the pigment obtained from the steamed powdered product, and the pigment obtained from raw purple sweet potato (in terms of a color value of 80) was added, and the color tone was visually observed Observed. Table 1 shows the results. Further, the color value of each raw material was calculated from the amount of the collected dye. [Table 1] Color value: It means the density (color strength) of a dye, generally measured by a spectrophotometer, and expressed by converting the measured value to a value of 10% density. In general, the measurement of the spectrophotometer is performed by adjusting the concentration of the dye so that the absorbance at the maximum absorption wavelength is in the range of 0.2 to 0.7. For example, when the absorbance (λmax OD) at the maximum absorption wavelength is 0.5 at a dye concentration of 0.1 volume / weight%, 10 ÷ 0.1 =
100 Color value = 0.5 × 100 = 50 From Table 1, it can be seen that the dye prepared by the method of the present invention exhibited a bright red color tone similar to the dye prepared from raw purple sweet potato, and also showed a high pigment content. In comparison, the steamed powder did not become a bright red pigment. The reason why the pigment content of the steamed powder product showed a high value was that a change due to heat was observed, the color tone became yellow, and the yellow component was also included in the raw material color value. Comparative Example 2 5 kg of purple sweet potato "Ayamurasaki" was sliced into slices having a thickness of 3 mm, a width of 2 mm and a length of 20 mm using a slicer, and dried for 5 days by the sun to obtain 2 kg of a sun-dried purple sweet potato. In addition, 5 kg of the above-mentioned “Ayamurasaki” square shredded material was dried with hot air of 80 ° C. for 3 hours using a dryer,
1.8 kg of hot-air dried purple sweet potato was obtained. Using a sun-dried product and a hot-air dried product as a dye raw material, a dye was produced by the method of Example 1, and the color tone was visually observed. Table 2 shows the results. [Table 2] From Table 2, the dye produced by the method of the present invention turned bright red. However, the pigment produced from the extracted raw material subjected to sun drying and hot air drying did not become bright red because the color tone was changed by drying. Comparative Example 3 The purple sweet potato of Example 1 "Ayamurasaki" 70 g of the pulverized powder obtained by passing the dried and pulverized product through a 32-mesh sieve, and the raw purple sweet potato having the same amount of pigment as 70 g of the pulverized powdered product Ayamurasaki ”1Kg is cut into 3-5mm squares,
Pour into 10 l of 0.5% by weight sulfuric acid aqueous solution and extract
The dye was extracted at 60 ° C for 60 minutes. FIG. 1 shows the relationship between the time and the amount of the extracted pigment. From FIG. 1, it was found that in the production method according to the present invention, the extraction was completed in about 1/6 of the production method using raw purple sweet potato. Comparative Example 4 Dry Sweet Potato "Ayamurasaki" of Example 1
00 g was added to an extract of 1 liter of a 0.5% by weight aqueous sulfuric acid solution, and purple sweet potato was extracted at 45 ° C. for 10 minutes to obtain 800 g of an extracted pigment solution. Similarly, 100 g of the steamed powdered product which had been steamed by the method of Comparative Example 2 and then turned into a dry powder, and 300 g of fresh purple sweet potato were similarly extracted at 45 ° C. for 10 minutes to obtain a pigment solution. These extracts were filtered through a filter paper with a Φ9 cm suction filter (ADVANTEC FILTER PAPER).
5C) was performed, and the time from the start of filtration of the extract to the end of filtration was measured. [Table 3] As shown in Table 3, the time required for filtration was shorter in the production method according to the present invention than in the production method using steamed powder or raw purple sweet potato. As is evident from Comparative Examples 3 and 4, the production method according to the present invention can greatly reduce the time required for production as compared with other production methods, and can be produced industrially advantageously. . COMPARATIVE EXAMPLE 5 The dried and crushed purple sweet potato "Ayamurasaki" of Example 1 and the steamed purple sweet potato "Ayamurasaki" were dried with a drum dryer and then stored in a warehouse at 15 ° C. or lower. Table 4 shows the relationship between the residual ratio (%) of the contained pigment and the rot by the naked eye when the sweet potato was stored in a humidified refrigerator at 15 ° C. in a supersaturated state. [Table 4] From Table 4, it can be seen that the pigment produced by the production method according to the present invention has almost no deterioration in the quality of the pigment as compared with the pigment produced by the production method using raw sweet potato, and can be stored for a long time. I understand. Example 2 1 kg of the dried and ground purple sweet potato "Ayamurasaki" of Example 1 was poured into an extract of 10 l of a 50% by volume aqueous alcohol solution containing 0.01% by weight of sulfuric acid, extracted at 25 ° C for 60 minutes, and filtered. Thus, 8.5 kg of an extract was obtained by removing insoluble solids. The solution was concentrated to 5 liters, and Diaion HP-20 was added.
(Adsorption resin manufactured by Mitsubishi Kasei Kogyo Co., Ltd.) After adsorbing on 500 ml, washing with water was performed, and the adsorbed dye was eluted using 500 ml of 58 vol% ethyl alcohol. The obtained dye solution was concentrated to 80 g with a vacuum concentrator, 3 g of glycerin fatty acid ester and 2 g of sucrose fatty acid ester
g, edible oil 16 g, gum arabic 40 g, 95% ethyl alcohol 20 g, citric acid 10 g, glycerin 20
g of water and 9 g of water were added and stirred and mixed with a homodisper to obtain 200 g of a double emulsified dye liquid of purple sweet potato. The obtained purple sweet potato pigment was colored in jelly and exhibited a clear red color when immersed in syrup, and did not cause any color change or color flow to the syrup even after being kept at room temperature for one month. According to the present invention, the time required for the production of purple sweet potato can be greatly reduced as compared with the conventional method for producing a pigment, and the interference by oxidase which has been involved in the discoloration and discoloration of the pigment can be obtained. Disappears. Moreover, since the purple sweet potato can be stored for a long period of time by making it into a dry and pulverized product, it is not necessary to concentrate the production of the pigment, and the purple sweet potato with excellent color tone can be produced efficiently and industrially advantageously. I can do it. [0039]
【図面の簡単な説明】
【図1】抽出工程での時間の経過による色素の抽出液へ
の移行量を示すグラフであり、縦軸は色素量、横軸は時
間を示す。
【符号の説明】
(1) 抽出原料:紫さつまいも乾燥粉砕物
(2) 抽出原料:生の紫さつまいも
t 時間(分)
V 色素量 抽出液の色価×液量BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a graph showing a transfer amount of a dye to an extract over time in an extraction step, wherein the vertical axis indicates the amount of the dye and the horizontal axis indicates time. [Explanation of Signs] (1) Extraction raw material: dried and dried purple sweet potato (2) Extracted raw material: raw purple sweet potato t Time (minutes) V Pigment amount Color value of extraction liquid x liquid amount
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C09B 61/00 A23L 1/275 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) C09B 61/00 A23L 1/275
Claims (1)
量10%以下に乾燥し粉砕した甘しょ農林47号を用い
ることを特徴とする紫さつまいも色素の製造方法。(57) [Claims] [Claim 1] Moisture content in the production of purple sweet potato
A method for producing a purple sweet potato pigment, comprising using sweet potato Norin 47 dried and crushed to an amount of 10% or less .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP07289896A JP3408919B2 (en) | 1996-03-27 | 1996-03-27 | Method for producing purple sweet potato pigment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP07289896A JP3408919B2 (en) | 1996-03-27 | 1996-03-27 | Method for producing purple sweet potato pigment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH09255889A JPH09255889A (en) | 1997-09-30 |
| JP3408919B2 true JP3408919B2 (en) | 2003-05-19 |
Family
ID=13502637
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP07289896A Expired - Fee Related JP3408919B2 (en) | 1996-03-27 | 1996-03-27 | Method for producing purple sweet potato pigment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3408919B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102391669A (en) * | 2011-11-08 | 2012-03-28 | 北京工业大学 | Natural haematochrome extracted from sweet potato skin and preparation method thereof |
| CN102391667A (en) * | 2011-08-30 | 2012-03-28 | 河南中大生物工程有限公司 | Purification method of purple sweet potato pigment |
| CN102604424A (en) * | 2012-02-27 | 2012-07-25 | 河北科技大学 | Method for extracting anthocyanins from purple sweet potato |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1300255C (en) * | 2003-12-23 | 2007-02-14 | 西南师范大学 | Extracting process for purple sweet potato antocynidin and mucin |
| JP2007217583A (en) * | 2006-02-17 | 2007-08-30 | Toyo Ink Mfg Co Ltd | Method for producing butterfly flower extract and butterfly flower extract |
| CN100460470C (en) * | 2006-11-10 | 2009-02-11 | 华南师范大学 | Extraction method of purple sweet potato pigment |
| JP5137220B1 (en) * | 2012-02-15 | 2013-02-06 | 株式会社奄美大島開運酒造 | Method for producing solder anthocyanin pigment extract |
| CN103450703B (en) * | 2013-09-25 | 2014-11-05 | 宁波海通食品科技有限公司 | Method for preparing high-purity taste-removing purple sweet potato pigment |
| CN120604830A (en) * | 2015-05-12 | 2025-09-09 | 三荣源有限公司 | Anthocyanin dye preparations |
| WO2020203781A1 (en) * | 2019-03-29 | 2020-10-08 | 三栄源エフ・エフ・アイ株式会社 | Dye composition |
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1996
- 1996-03-27 JP JP07289896A patent/JP3408919B2/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102391667A (en) * | 2011-08-30 | 2012-03-28 | 河南中大生物工程有限公司 | Purification method of purple sweet potato pigment |
| CN102391667B (en) * | 2011-08-30 | 2014-02-12 | 河南中大生物工程有限公司 | A kind of purification method of purple sweet potato pigment |
| CN102391669A (en) * | 2011-11-08 | 2012-03-28 | 北京工业大学 | Natural haematochrome extracted from sweet potato skin and preparation method thereof |
| CN102604424A (en) * | 2012-02-27 | 2012-07-25 | 河北科技大学 | Method for extracting anthocyanins from purple sweet potato |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH09255889A (en) | 1997-09-30 |
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