JP4235113B2 - Method for producing french fries with improved texture and oil content - Google Patents
Method for producing french fries with improved texture and oil content Download PDFInfo
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- JP4235113B2 JP4235113B2 JP2003565259A JP2003565259A JP4235113B2 JP 4235113 B2 JP4235113 B2 JP 4235113B2 JP 2003565259 A JP2003565259 A JP 2003565259A JP 2003565259 A JP2003565259 A JP 2003565259A JP 4235113 B2 JP4235113 B2 JP 4235113B2
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Classifications
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L19/00—Products from fruits or vegetables; Preparation or treatment thereof
- A23L19/10—Products from fruits or vegetables; Preparation or treatment thereof of tuberous or like starch containing root crops
- A23L19/12—Products from fruits or vegetables; Preparation or treatment thereof of tuberous or like starch containing root crops of potatoes
- A23L19/18—Roasted or fried products, e.g. snacks or chips
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
- A23P20/00—Coating of foodstuffs; Coatings therefor; Making laminated, multi-layered, stuffed or hollow foodstuffs
- A23P20/10—Coating with edible coatings, e.g. with oils or fats
- A23P20/12—Apparatus or processes for applying powders or particles to foodstuffs, e.g. for breading; Such apparatus combined with means for pre-moistening or battering
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Preparation Of Fruits And Vegetables (AREA)
Description
1.技術分野
油ちょう後のフライドポテト中の油の含有量を低減させ、好ましい食感を有するフライドポテトの製造方法に関する。
2.背景技術
油ちょう食品の中でも馬鈴薯を油ちょうして得られるフライドポテトは、日本における欧米食文化の広がりを背景に、ファーストフード、ファミリーレストラン等の外食産業に限らず、弁当惣菜業界、市販冷凍食品業界、スナック菓子業界に至るまで幅広く商品化されている。また、揚げたてのフライドポテトは、その風味だけでなく、表面のサクサクとしたクリスピー感や、内部のホクホクとした食感が好まれるため、料理の付け合わせやおやつとして、一般家庭内でも幅広く使用されており、その消費量は増加の一途を辿っている。
しかしながら、フライドポテトは油ちょう品であるために油の接取量が多くなりやすく、カロリーが高い食品でもあることから、肥満に代表される生活習慣病の原因になることが懸念されている。また、フライドポテト中に含まれる油分が表面にしみ出すこと、サクサクとした食感が失われること、味そのものが劣化すること、しみ出した油により包装容器を汚してしまうこと等、商品価値の低下を招く経時変化が生じ易いという欠点を有している。
これらの問題を解決する手段として、フライドポテト中の油の含有量を低減させることが挙げられ、これまでに幾つかの方法が提案されている。
特開平6−141787号公報には、フライドポテトの吸油を抑制する方法として、大豆蛋白質を用いて油ちょうされるジャガイモ表面をコーティングするか、あるいは大豆蛋白質を成形生地又は衣に混合する方法が開示されている。しかしこの方法では吸油抑制効果は認められるものの、大豆蛋白独特の味や臭いがする、油ちょうによる着色や焦げが生じ易く、商品価値が低下してしまうという欠点があった。また、特開平3−259046号公報には、ゲル状アクトミオシンでコーティングするか、あるいは生地中に混合する方法が開示されている。しかしながらこの方法では、アクトミオシンの調製に手間が掛かること、コストが高いこと、吸油性以外には具体的な改良効果が認められないという欠点があった。
3.発明の開示
本発明者らによると、油ちょう前の馬鈴薯に対し、デキストリン還元物を含有した水溶液でブランチング処理を行なうことにより、油ちょう後のフライドポテト中の油の含有量を低減させ、更に好ましい食感となることを見出し、本発明を完成するに至った。
本発明の課題を解決する手段は以下の通りである。
第一に、油ちょう前に、デキストリン還元物を含有する水溶液を用いて馬鈴薯のブランチング処理を行う工程を含む、フライドポテトの製造方法。
第二に、固形分含有量が0.1〜25.0重量%のデキストリン還元物水溶液中で、馬鈴薯をボイルブランチングし、次いで油ちょう処理する、フライドポテトの製造方法。
第三に、固形分含有量が5.0〜50.0重量%のデキストリン還元物水溶液を用いて、馬鈴薯を当該水溶液中に浸漬するか、もしくは当該水溶液を馬鈴薯に噴霧した後、馬鈴薯をスチームブランチングし、次いで油ちょう処理する、フライドポテトの製造方法。
第四に、デキストリン還元物が、DE20未満のデキストリンの水素化物である、第一から第三の何れか一つに記載のフライドポテトの製造方法。
第五に、デキストリン還元物が、固形物当り糖重合度20以上の糖類の水素化物を50.0重量%以上含有するものである、第四に記載のフライドポテトの製造方法。
本発明は、馬鈴薯の産地や品種によって特に限定されることはなく、例えば、北海黄金、豊白、男爵、早生白、メークイン、農林1号、北光、紅丸、出島、西豊、ラセット・バーバンク等、国内産、外国産を問わず使用することができる。
本発明において、ブランチング処理時の馬鈴薯の形状は特に問われないため、加工のし易さや食べ易さの点を考慮して、適当な大きさや形状にカットしたものをそのままブランチング処理するか、必要に応じて皮むきをした馬鈴薯を、スティック状や薄くスライスした平板状などにしてブランチング処理しても良い。
本発明で使用するデキストリン還元物は、澱粉を原料として、酵素、酸、アルカリ、加熱等の処理操作を行なって得られるDE(Dextrose Equivalent)が20未満の澱粉分解物であるデキストリンを、公知の方法で水素化することで得ることができる。
本発明で使用するデキストリン還元物の原料は、地上澱粉、地下澱粉等の特段の制限はなく、上記した範囲内のDE値を持ったデキストリンを還元したものであれば十分に使用可能である。
本発明で使用するデキストリン還元物は、DE20未満のデキストリンを還元したものの使用が好ましいが、得られたフライドポテト中の油の含有量の低減、食感の改良、操作の効率、取扱いの容易さ等から、DE3〜15程度のデキストリンを還元したものが更に好ましく、DE5〜12程度のデキストリンを還元したものが最も好ましい。
DEが20以上のデキストリンを還元したデキストリン還元物を用いた場合、本発明に係るフライドポテトの食感改良や油の含有量の低減などの効果が十分に得られないことがある。またDEが3未満のデキストリンを還元したデキストリン還元物を用いた場合、上述の効果が得られないことがあるだけでなく、ブランチングに用いる水溶液の調製が困難であり、水溶液の粘性が高いため、ブランチング処理時の取扱いが困難となる場合が有る。
本発明で使用するデキストリン還元物は、上記DEを有したデキストリンを還元したものの使用が好ましいが、本発明の効果を更に効果的に得るには、デキストリン還元物の固形物当り、糖重合度が20以上の糖類の水素化物が50.0重量%以上含まれたものが更に好ましく、糖重合度が20以上の糖類の水素化物が70.0重量%以上含まれたものが最も好ましい。
本発明で使用するデキストリン還元物は、デキストリン及びその還元物の老化を防止し、それに伴う本発明の作用効果の低下を防止する観点から、分岐構造を多く有していることが好ましく、例えば、アミロペクチンの含有量の高い澱粉を原料としたり、クロマトグラフ、膜濾過等の分離手段により分岐構造部分と直鎖構造部分を分離し、分岐構造部分を多く含有させたものが有利に使用可能である。
フライドポテトの製造では、馬鈴薯を油ちょうする前にブランチングと呼ばれる処理が行われ、その条件はフライドポテト用にカットされた馬鈴薯の大きさに応じて異なるが、一般的な手法として、約60〜100℃に加熱した熱湯中に約0.5〜20分間程度浸漬するボイルブランチングや、約90〜110℃の蒸気に約1〜10分間程度ブランチングするスチームブランチング等が挙げられる。
ブランチング処理の一般的な目的として、馬鈴薯中に含まれる酵素の失活、馬鈴薯の褐変防止、油ちょう後のフライドポテトの食感改善、油ちょう時の馬鈴薯の火の通りを良くする、等がある。
本発明の実施にあたり採用可能なブランチング処理の方法として、例えば、デキストリン還元物を含有した水溶液中に、適当な大きさにカットした馬鈴薯を加えて加熱処理を行う、ボイルブランチングが挙げられる。
ボイルブランチングを行う場合、使用するデキストリン還元物を含有した水溶液の固形分含有量は、0.1〜25.0重量%、好ましくは5.0〜15.0重量%に調製されたものが良い。
水溶液中の固形分含有量が25.0重量%を超えても、フライドポテトの食感改良や、フライドポテト中の油の含有量の低減に一定の効果は認められるが、馬鈴薯表面が過度にべたついたり、油ちょう時に馬鈴薯同士が結着を起こす等の影響が現れ易くなってしまう。また、水溶液中の固形分含有量が0.1重量%を下回ると、本発明の効果が十分に得られなくなるため好ましくない。
ボイルブランチングを行う際の水溶液の温度とブランチング処理の時間は、通常は約60〜100℃の温度条件で約0.5〜20分程度であり、好ましくは約90〜100℃の温度条件で約0.5〜5分程度であるが、馬鈴薯の種類、品質、形状、油ちょう前の馬鈴薯への火の通し加減等を加味し、適宜変更することが可能である。
また、本発明では、ブランチング処理液に用いられる成分が熱に強く老化しにくいデキストリン還元物であるため、ブランチング処理液を沸騰状態まで加熱して用いても問題なく使用することが可能である。
本発明の実施にあたり採用可能なブランチング処理のその他の方法として、例えば、スチームブランチングを採用することも可能である。
スチームブランチングを行う場合、適当な大きさにカットした馬鈴薯をデキストリン還元物を含有した水溶液中に浸漬させるか、もしくはデキストリン還元物を含有した水溶液を直接噴霧し、馬鈴薯の表面がまんべんなくデキストリン還元物を含有する水溶液で覆われた後、馬鈴薯をスチームで加熱処理することで、本発明に係る効果を得ることが出来る。
スチームブランチングを行う場合、使用するデキストリン還元物を含有した水溶液の固形分含有量は、5.0〜50.0重量%、好ましくは10.0〜30.0重量%に調製されたものが良い。
水溶液中の固形分含有量が50.0重量%を超えても、フライドポテトの食感改良や、フライドポテト中の油の含有量の低減に一定の効果は認められるが、馬鈴薯表面がべたつく、油ちょう時に馬鈴薯同士が結着を起こし易い、水溶液の調製が困難である等、問題点が多い。また、水溶液中の固形分含有量が5.0重量%を下回ると、本発明の効果が十分に得られなくなる可能性が高い。
スチームブランチング法を採用する際、カットした馬鈴薯をデキストリン還元物水溶液中に浸漬するか、もしくはカットした馬鈴薯にデキストリン還元物水溶液を噴霧するが、浸漬時間や噴霧時間について特に制限はなく、カットした馬鈴薯の表面にデキストリン還元物がまんべんなく覆われる程度で十分である。また、浸漬もしくは噴霧に用いる際のデキストリン還元物水溶液の温度について特に制限はなく、常温でも加熱した物でも良い。
浸漬処理もしくは噴霧処理を終えた馬鈴薯は、そのまま直ちにスチーム処理を行うが、その条件として通常はスチーム温度90〜110℃で1〜10分程度であるが、スチーム温度、スチーム圧、処理時間等のスチーム処理の諸条件は、馬鈴薯の種類、品質、形状、油ちょう前の馬鈴薯への火の通し加減等を加味し、適宜変更することが可能である。
デキストリン還元物水溶液を用いて馬鈴薯のブランチング処理を行うことで、馬鈴薯表面の澱粉質とデキストリン還元物との間で相互作用が生じ、馬鈴薯表面に高粘度化された皮膜状物質が形成されると考えられ、その結果、油ちょう後のフライドポテト表面のサクサクとした食感、内部のホクホクとした食感、フライドポテト中の油の含有量の低減等、本発明に係る効果を得ることができると考えられる。
本発明に係るブランチング処理を施した馬鈴薯は、公知の調理方法に従って製造することで、好ましい食感を有し、油の含有量が低減したフライドポテトを得ることが可能であり、例えば、ブランチング処理後そのまま油ちょうを行い製品に仕上げる方法や、油ちょうを2回に分けて行い、一次油ちょうで一旦半製品状態とし、次いで二次油ちょうを行い製品に仕上げる方法、あるいは一次油ちょうで一旦半製品状態としたものをオーブンや電子レンジで製品に仕上げる方法、等の調理方法を採用することが可能である。
本発明に係るフライドポテトの製造に当たり、ブランチング処理した後の馬鈴薯の油ちょう処理は、1回もしくは複数回実施することが可能であるが、サクサクとした好ましい食感を得る上で、油ちょう処理を2回に分けて行うことが好ましい。
油ちょう処理の温度に特に制限は無いが、2回の油ちょう処理を行う場合、一次油ちょうは約150〜180℃程度とやや低温で、2次油ちょうは約160〜200℃と一次油ちょう時の温度よりもやや高温で油ちょう処理することが好ましい。また、一次油ちょうが終了した後は、そのまますぐに二次油ちょうを行っても良いが、一次油ちょう品の状態で一旦保存し、商品とする直前の段階で二次油ちょうを行っても良い。
油ちょう処理の時間に関しては、馬鈴薯の種類、カットした馬鈴薯の大きさ、希望する揚げ上がりの状態でそれぞれ異なるため特に限定はないが、通常、数10秒〜10分程度である。
また、一次油ちょうにより半製品状態にした馬鈴薯を冷凍保存することで、長期間保存可能で、且つ通常よりも短時間で製品に仕上げることが可能な冷凍フライドポテトとして取り扱うことが可能である。この方法によって得られる冷凍フライドポテトは、所望の期間冷凍保存をした後、必要に応じ解凍するか冷凍状態のままで二次油ちょうを行うか、オーブンや電子レンジによる加熱を行うことで、本発明に係る効果を有したフライドポテトを製造することが可能である。
上述の方法に従えば、半製品の状態での長期保存や輸送が可能であり、最終形態であるフライドポテトを製造する際、より短期間の油ちょうでフライドポテトを製造することが出来るという利点も有することから、家庭用冷凍食品、ファーストフード店等でも、本発明に係る効果を有したフライドポテト製品を容易に得ることができる。
油ちょう処理で使用する油については、一般に油ちょう処理に用いられている油脂類であればいずれも使用可能であり、植物油、動物油、など各種油脂類を単独もしくは混合して使用しても良い。
本発明に係るフライドポテトの製造方法において、ブランチング処理に使用するデキストリン還元物の水溶液中に、調味を目的として種々の調味料、甘味料、アミノ酸をはじめとする核酸系調味料、香辛料、リン酸塩、などの各種添加剤を適宜混合しても良い。
4.発明の効果
本発明に従ってフライドポテトを製造する事により、通常のブランチング処理を行って製造されるフライドポテトよりも、油ちょう後に含まれるフライドポテト中の油の含有量を低減させ、好ましい食感を有するフライドポテトを製造することが可能となった。
5.発明を実施するための最良の形態
以下に実施例を挙げて本発明を詳細に説明するが、本発明の技術的範囲は以下の例に制限されるものではない。また、以下に示す例において、%は特に断りが無い限り重量%を表すものとする。また、実施例及び比較例の油ちょう処理では、市販のサラダ油を使用した。
[実施例1]
フライドポテトの原料として男爵芋を用い、皮を剥き、芽を除去した後、縦×横×長さが、おおよそ1cm×1cm×5〜8cmの大きさにカットしたものを300g用意した。
デキストリン還元物として、DEが約8のデキストリンの還元物(商品名:PO−10、東和化成工業株式会社製)を用い、固形分含有量が10.0重量%のデキストリン還元物水溶液を調製した。用意したデキストリン還元物の固形物当り、糖重合度20以上の糖類の水素化物の含有量は75.0重量%であった。
カットした男爵芋を、沸騰したデキストリン還元物水溶液中に添加し、3分間ボイルブランチングした。
ブランチング処理後、男爵芋を取出して水切りを行い、室温になるまで放冷した後、一次油ちょうとして160〜170℃で2分間油ちょうを行った。油ちょう後、室温で10分間放冷し、そのまま−30℃の冷蔵庫にて3日間冷凍保存した。
冷凍保存された一次油ちょう済みの男爵芋を冷凍庫から取出して直ちに、180〜190℃で2分間の二次油ちょうを行い、男爵芋のフライドポテトを製造した。
[実施例2]
フライドポテトの原料として北海黄金を用い、皮を剥き、芽を除去した後、縦×横×長さが、おおよそ1cm×1cm×5〜8cmの大きさにカットしたものを300g用意した。
実施例1と同様のデキストリン還元物を用いて、固形分含有量が10.0重量%のデキストリン還元物水溶液を調製した。
カットした北海黄金を、沸騰したデキストリン還元物水溶液中に添加し、3分間ボイルブランチングした。
ブランチング処理後、男爵芋を取出して水切りを行い、室温になるまで放冷した後、一次油ちょうとして160〜170℃で2分間油ちょうを行った。油ちょう後、室温で10分間放冷し、そのまま−30℃の冷蔵庫にて3日間冷凍保存した。
冷凍保存された一次油ちょう済みの北海黄金を冷凍庫から取出して直ちに、180〜190℃で2分間の二次油ちょうを行い、北海黄金のフライドポテトを製造した。
[実施例3]
ブランチングに用いるデキストリン還元物水溶液の固形分含有量を1.0重量%とした以外は、実施例2と同様の方法で、北海黄金のフライドポテトを製造した。
[実施例4]
ブランチングに用いるデキストリン還元物水溶液の固形分含有量を5.0重量%とした以外は、実施例2と同様の方法で、北海黄金のフライドポテトを製造した。
[実施例5]
ブランチングに用いるデキストリン還元物水溶液の固形分含有量を10.0重量%とした以外は、実施例2と同様の方法で、北海黄金のフライドポテトを製造した。
[実施例6]
ブランチングに用いるデキストリン還元物水溶液の固形分含有量を15.0重量%とした以外は、実施例2と同様の方法で、北海黄金のフライドポテトを製造した。
[実施例7]
フライドポテトの原料として北海黄金を用い、皮を剥き、芽を除去した後、縦×横×長さが、おおよそ1cm×1cm×5〜8cmの大きさにカットしたものを300g用意した。
実施例1と同様のデキストリン還元物を用いて、固形分含有量が20.0重量%のデキストリン還元物水溶液を調製した。
カットした北海黄金を、25℃に調節したデキストリン還元物水溶液に1分間浸漬した。
浸漬液から取出して軽く水を切りを行った北海黄金を、予め100℃に加熱した蒸し器内に設置し、スチーム温度を100℃に維持した状態で、3分間スチームブランチングを行った。
スチームブランチング後、北海黄金を取出して室温になるまで放冷した後、一次油ちょうとして160〜170℃で2分間油ちょうを行った。油ちょう後、室温で10分間放冷し、そのまま−30℃の冷蔵庫にて3日間冷凍保存した。
冷凍保存された一次油ちょう済みの馬鈴薯を冷凍庫から取出して直ちに、180〜190℃で2分間の二次油ちょうを行い、北海黄金のフライドポテトを製造した。
[比較例1]
ブランチングに用いる水溶液として、何も添加していない水を用いた以外は、実施例1と同様の方法で、男爵芋のフライドポテトを製造した。
[比較例2]
ブランチングに用いる水溶液として、DEが約8のデキストリンを用いて調製した、固形分含有量が10.0重量%のデキストリン水溶液を用いた以外は、実施例1と同様の方法で、男爵芋のフライドポテトを製造した。
[比較例3]
ブランチングに用いる水溶液として、還元澱粉糖化物(商品名:PO−20、東和化成工業株式会社製)を用いて調製した、固形分含有量が10.0重量%の還元澱粉糖化物水溶液を用いた以外は、実施例1と同様の方法で、男爵芋のフライドポテトを製造した。
本比較例で用いた還元澱粉糖化物PO−20は、DEが約21の澱粉分解物の還元物であり、固形物当りに含まれる糖重合度20以上の糖類の水素化物の含有量は26.0重量%であった。
[比較例4]
ブランチングに用いる水溶液として、マルチトール(商品名:レシス、東和化成工業株式会社製)を用いて調製した、固形分含有量が10.0重量%のマルチトール水溶液を用いた以外は、実施例1と同様の方法で、男爵芋のフライドポテトを製造した。
[比較例5]
ブランチングに用いる水溶液として、マルトース(商品名:サンマルト、株式会社林原生物化学研究所製)を用いて調製した、固形分含有量が10.0重量%のマルトース水溶液を用いた以外は、実施例1と同様の方法で、男爵芋のフライドポテトを製造した。
[比較例6]
ブランチングに用いる水溶液として、ソルビトール(商品名:ソルビット、東和化成工業株式会社製)を用いて調製した固形分含有量が10.0重量%のソルビトール水溶液を用いた以外は、実施例1と同様の方法で、男爵芋のフライドポテトを製造した。
[比較例7]
ブランチングに用いる水溶液として、何も添加していない水を用いた以外は、実施例2と同様の方法で、北海黄金のフライドポテトを製造した。
[比較例8]
ブランチングに用いる水溶液として、DEが約8のデキストリンを用いて調製した、固形分含有量が10.0重量%のデキストリン水溶液を用いた以外は、実施例2と同様の方法で、北海黄金のフライドポテトを製造した。
[比較例9]
ブランチングに用いる水溶液として、マルチトール(商品名:レシス、東和化成工業株式会社製)を用いて調製した、固形分含有量が10.0重量%のマルチトール水溶液を用いた以外は、実施例2と同様の方法で、北海黄金のフライドポテトを製造した。
[比較例10]
ブランチングに用いる水溶液として、マルトース(商品名:サンマルト、株式会社林原生物化学研究所製)を用いて調製した、固形分含有量が10.0重量%のマルトース水溶液を用いた以外は、実施例2と同様の方法で、北海黄金のフライドポテトを製造した。
[比較例11]
ブランチングに用いる水溶液として、何も添加していない水を用いた以外は、実施例7と同様の方法で、北海黄金のフライドポテトを製造した。
[比較例12]
ブランチングに用いる水溶液として、DEが約8のデキストリンを用いて調製した、固形分含有量が20.0重量%のデキストリン水溶液を用いた以外は、実施例7と同様の方法で、北海黄金のフライドポテトを製造した。
[比較例13]
ブランチングに用いる水溶液として、還元澱粉糖化物(商品名:PO−20、東和化成工業株式会社製)を用いて調製した、固形分含有量が20.0重量%の還元澱粉糖化物水溶液を用いた以外は、実施例7と同様の方法で、北海黄金のフライドポテトを製造した。
[比較例14]
ブランチングに用いる水溶液として、マルチトール(商品名:レシス、東和化成工業株式会社製)を用いて調製した、固形分含有量が20.0重量%のマルチトール水溶液を用いた以外は、実施例7と同様の方法で、北海黄金のフライドオテトを製造した。
[比較試験1]
(1)フライドポテト中の油の含有量の測定
ソックスレー法によって、発明品と比較品のフライドポテトの油分抽出を行い、フライドポテト中の油の含有量を求めた。
各実施例及び比較例にて製造した発明品と比較品のフライドポテトは、それぞれの油ちょう終了後、金網の上に5分間静置して油きりを行い、次いでキッチンペーパー上で室温になるまで放冷し、フライドポテトからしみ出す余分な油分を除去したものを、乳鉢で均一になるまで磨り潰し、これを測定用サンプルとした。
測定用サンプル中から無作為に約8g程度を採取したものを1検体とし、10検体分を無作為に採取した。採取したサンプルは、円筒形の乾燥濾紙内にこぼれないように入れた。この時の乾燥濾紙のみの重量をAとし、乾燥濾紙とサンプルの合計重量をBとした。
乾燥濾紙内にサンプルを入れた状態で、60℃で12時間、減圧乾燥を行い、乾燥処理後の濾紙とサンプルの合計重量を計量し、この値をCとした。
減圧乾燥したサンプルは、ジエチルエーテルを用いて、ソックスレー管の中で油分抽出を10時間行った。
抽出を終えたサンプルは、90℃で5時間の減圧乾燥を行い、サンプル重量を計測し、この値をDとした。
フライドポテト中の油の含有量は、以下の計算式に従い、フライドポテト全重量当りの重量%で求めた。
フライドポテト中の油の含有量(wt%)=(C−D)/(B−A)×100
[比較試験2]
(2)フライドポテトの食感
本発明に係るフライドポテトについて、フライドポテト表面のサクサク感と、フライドポテト内部のホクホク感を、水でブランチングして製造されたフライドポテトを基準品として、訓練されたパネリスト10名の官能検査による相対評価を行った。
男爵芋を用いた実施例1及び比較例1〜比較例6に係るフライドポテトについては、比較例1で製造したフライドポテトを基準品とした。
北海黄金を用いた実施例2〜実施例6及び比較例7〜比較例10に係るフライドポテトについては、比較例7で製造したフライドポテトを基準品とした。
北海黄金を用いた実施例7及び比較例11〜比較例14に係るフライドポテトについては、比較例11で製造したフライドポテトを基準品とした。
フライドポテト表面のサクサク感については、基準品と比べて非常に良い:◎、基準品よりも良い:○、基準品と同等:△、基準品よりも劣る:×、で評価し、最も得票の多い評価を官能検査の結果とした。
フライドポテト内部のホクホク感については、基準品と比べて非常に良い:◎、基準品よりも良い:○、基準品と同等:△、基準品よりも劣る:×、で評価し、最も得票の多い評価を官能検査の結果とした。
1. TECHNICAL FIELD The present invention relates to a method for producing french fries having a favorable texture by reducing the content of oil in french fries after oil.
2. BACKGROUND ART French fries obtained from potatoes in oil-boiled foods are not limited to the food service industry such as fast food and family restaurants, but also in the bento and other frozen foods and commercial frozen foods industries. It has been widely commercialized, ranging from the snack confectionery industry. In addition, freshly fried French fries are used not only for their flavor, but also for their crispy crispy surface and the texture of the inside, so they are widely used in homes as a garnish and snack. The amount of consumption continues to increase.
However, since French fries are an oily product, the amount of oil to be taken in tends to increase, and since it is a food with high calories, there is concern that it may cause lifestyle-related diseases such as obesity. In addition, the oil content in French fries oozes out on the surface, the crispy texture is lost, the taste itself deteriorates, and the packaging container is soiled by the exuded oil. There is a drawback that a change with time is likely to occur.
As a means for solving these problems, it is possible to reduce the content of oil in the french fries, and several methods have been proposed so far.
Japanese Patent Application Laid-Open No. 6-141787 discloses a method for suppressing the oil absorption of french fries by coating the surface of potato oiled with soy protein or mixing soy protein into a molded dough or clothing. Has been. However, although this method has an oil absorption suppressing effect, it has a disadvantage that it has a unique taste and smell of soy protein, is likely to be colored or burnt by oil, and the commercial value is lowered. JP-A-3-259046 discloses a method of coating with gel actomyosin or mixing in dough. However, this method has the disadvantages that it takes time and effort to prepare actomyosin, the cost is high, and no specific improvement effect other than oil absorption is observed.
3. DISCLOSURE OF THE INVENTIONAccording to the present inventors, the potato before cooking oil is subjected to a blanching treatment with an aqueous solution containing a dextrin reduced product, thereby reducing the content of oil in the french fries after cooking oil, The present inventors have found that the texture is more favorable and have completed the present invention.
Means for solving the problems of the present invention are as follows.
1stly, the manufacturing method of French fries including the process of performing the branching process of a potato using the aqueous solution containing a dextrin reduction product before oiling.
Second, a method for producing french fries, in which potato is boiled and then oil-boiled in a dextrin-reduced aqueous solution having a solid content of 0.1 to 25.0% by weight.
Thirdly, using a dextrin-reduced aqueous solution having a solid content of 5.0 to 50.0% by weight, the potato is immersed in the aqueous solution or sprayed on the potato, and then the potato is steamed. A method for producing french fries, which is blanched and then treated with oil.
Fourth, the method for producing french fries according to any one of the first to third, wherein the dextrin reduction product is a hydride of dextrin having a DE of less than 20.
Fifth, the method for producing french fries according to the fourth aspect, wherein the dextrin reduced product contains 50.0% by weight or more of a saccharide hydride having a sugar polymerization degree of 20 or more per solid.
The present invention is not particularly limited by the production area and variety of potatoes. For example, North Sea Golden, Toyohaku, Baron, Hakusei Haku, Makein, Norin 1, Kitako, Benimaru, Dejima, Nishitoyo, Russet It can be used regardless of domestic or foreign production such as Burbank.
In the present invention, since the shape of the potato at the time of the blanching process is not particularly limited, in consideration of the ease of processing and the ease of eating, what is cut into an appropriate size or shape is blanched as it is If necessary, the peeled potato may be blanched into a stick shape or a thinly sliced flat plate shape.
The dextrin reduced product used in the present invention is a known dextrin which is a starch degradation product having a DE (Dextrose Equivalent) of less than 20 obtained by performing a processing operation such as enzyme, acid, alkali, and heating using starch as a raw material. It can be obtained by hydrogenation by the method.
The raw material for the dextrin reduced product used in the present invention is not particularly limited, such as ground starch, underground starch, etc., and any dextrin having a DE value within the above range can be used sufficiently.
The reduced dextrin used in the present invention is preferably a reduced dextrin of less than DE 20, but the oil content in the resulting fried potato is reduced, the texture is improved, the efficiency of operation, the ease of handling. From the above, a product obtained by reducing a dextrin having a DE of about 3 to 15 is more preferable, and a product obtained by reducing a dextrin having a DE of about 5 to 12 is most preferable.
When a dextrin reduced product obtained by reducing a dextrin having a DE of 20 or more is used, effects such as improving the texture of the french fries according to the present invention and reducing the oil content may not be sufficiently obtained. In addition, when a dextrin reduced product obtained by reducing a dextrin having a DE of less than 3 is used, not only the above-mentioned effect may not be obtained, but also it is difficult to prepare an aqueous solution used for blanching, and the aqueous solution is highly viscous. In some cases, handling during branching processing becomes difficult.
The reduced dextrin used in the present invention is preferably a reduced dextrin having the above DE, but in order to obtain the effect of the present invention more effectively, the degree of sugar polymerization per solid dextrin reduced is More preferred are those containing 50.0% by weight or more of hydride of 20 or more sugars, and most preferred are those containing 70.0% by weight or more of hydride of sugars having a sugar polymerization degree of 20 or more.
The dextrin reduced product used in the present invention preferably has a lot of branched structures from the viewpoint of preventing aging of dextrin and the reduced product thereof, and preventing a reduction in the action and effect of the present invention associated therewith. Starch with a high amylopectin content can be used as a raw material, or a branched structure portion and a straight chain structure portion can be separated by separation means such as chromatograph and membrane filtration, and can be used advantageously. .
In the production of French fries, a process called blanching is performed before oiling the potato, and the conditions differ depending on the size of the potato cut for fries, but as a general method, about 60 Examples include boil blanching immersed in hot water heated to -100 ° C for about 0.5 to 20 minutes, steam blanching for about 1 to 10 minutes in steam of about 90 to 110 ° C, and the like.
General purposes of blanching treatment include deactivation of enzymes contained in potatoes, prevention of browning of potatoes, improvement of texture of french fries after oiling, improving the streets of potatoes during oiling, etc. There is.
As a blanching treatment method that can be employed in the practice of the present invention, for example, boil blanching is possible in which a potato cut into an appropriate size is added to an aqueous solution containing a dextrin reduction product and subjected to heat treatment.
When performing boil blanching, the solid content of the aqueous solution containing the dextrin reduction product used is 0.1 to 25.0% by weight, preferably 5.0 to 15.0% by weight. good.
Even if the solid content in the aqueous solution exceeds 25.0% by weight, a certain effect is observed in improving the texture of the french fries and reducing the oil content in the french fries, but the potato surface is excessive Effects such as stickiness and potato binding when oiling are likely to appear. On the other hand, if the solid content in the aqueous solution is less than 0.1% by weight, the effects of the present invention cannot be obtained sufficiently, which is not preferable.
The temperature of the aqueous solution and the blanching time during boil blanching are usually about 0.5 to 20 minutes under a temperature condition of about 60 to 100 ° C, preferably about 90 to 100 ° C. It is about 0.5 to 5 minutes, but it can be changed as appropriate in consideration of the type, quality, shape, igniting of the potato before cooking.
In the present invention, since the component used in the blanching treatment liquid is a dextrin reduction product that is resistant to heat and hardly aged, it can be used without any problem even if the blanching treatment liquid is heated to a boiling state. is there.
As another method of blanching processing that can be employed in the practice of the present invention, for example, steam blanching can be employed.
When steam blanching is performed, the potato cut into an appropriate size is immersed in an aqueous solution containing a dextrin reduction product, or directly sprayed with an aqueous solution containing a dextrin reduction product, and the surface of the potato is evenly reduced to a dextrin. After being covered with an aqueous solution containing, the effect of the present invention can be obtained by heat-treating the potato with steam.
When performing steam blanching, the solid content of the aqueous solution containing the dextrin reduction product used is 5.0 to 50.0% by weight, preferably 10.0 to 30.0% by weight. good.
Even if the solid content in the aqueous solution exceeds 50.0% by weight, a certain effect is observed in improving the texture of the french fries and reducing the oil content in the french fries, but the potato surface is sticky, There are many problems such as potatoes tending to bind to each other when oiling, and it is difficult to prepare an aqueous solution. Moreover, when solid content in aqueous solution is less than 5.0 weight%, possibility that the effect of this invention will not fully be acquired is high.
When adopting the steam blanching method, the cut potato is immersed in the dextrin reductate aqueous solution, or the cut potato is sprayed with the dextrin reductate aqueous solution. It is sufficient that the dextrin reduction product is evenly covered on the surface of the potato. Moreover, there is no restriction | limiting in particular about the temperature of the dextrin reductant aqueous solution at the time of using for immersion or spraying, The thing heated at normal temperature may be sufficient.
The potatoes that have been subjected to immersion treatment or spray treatment are immediately subjected to steam treatment as they are, and the conditions are usually about 1 to 10 minutes at a steam temperature of 90 to 110 ° C., but the steam temperature, steam pressure, treatment time, etc. Various conditions for the steam treatment can be changed as appropriate in consideration of the type, quality, shape, potatoes before and after cooking of the potatoes.
By blanching the potato with a dextrin-reduced aqueous solution, interaction occurs between the starch on the potato surface and the dextrin-reduced material, and a highly viscous film-like substance is formed on the potato surface. As a result, it is possible to obtain the effects according to the present invention, such as a crunchy texture on the surface of the fried potato after oiling, a texture with a frilled inside, a reduction in the content of oil in the fried potato, etc. It is considered possible.
The potatoes subjected to the blanching treatment according to the present invention can be obtained according to a known cooking method to obtain a fried food having a preferable texture and reduced oil content. After finishing the oil treatment, finish the product as it is, or make the product into two semi-finished products using the primary oil and then apply the secondary oil to finish the product. It is possible to adopt a cooking method such as a method of finishing a semi-finished product into a product with an oven or a microwave oven.
In the production of the french fries according to the present invention, the potato oil treatment after the blanching treatment can be carried out once or a plurality of times, but in order to obtain a crispy and preferable texture, The treatment is preferably performed in two steps.
There are no particular restrictions on the temperature of the oil treatment, but when performing the oil treatment twice, the primary oil content is about 150 to 180 ° C and the secondary oil content is about 160 to 200 ° C and the primary oil. It is preferable to perform the oil-contained treatment at a slightly higher temperature than the temperature at the time of the operation. In addition, after the primary oil is finished, the secondary oil can be used immediately. However, after the primary oil is stored in the state of the primary oil product, the secondary oil is applied just before making the product. Also good.
There are no particular limitations on the duration of the oil treatment, since it varies depending on the type of potato, the size of the cut potato, and the desired lifted state, but it is usually several tens of seconds to 10 minutes.
In addition, by storing frozen potatoes in a semi-finished product state with a primary oil butter, they can be stored as frozen fries that can be stored for a long period of time and can be finished into products in a shorter time than usual. Frozen french fries obtained by this method can be stored in a frozen state for a desired period of time, and then thawed as necessary, or secondarily oiled in a frozen state, or heated in an oven or microwave oven. It is possible to manufacture french fries having the effects according to the invention.
According to the above-mentioned method, long-term storage and transportation in the state of a semi-finished product are possible, and when manufacturing the final form of French fries, it is possible to manufacture French fries with a shorter period of oil. Therefore, it is possible to easily obtain a fried potato product having the effect according to the present invention even in a frozen food for home use, a fast food store or the like.
As the oil used in the oil treatment, any oil and fat generally used in the oil treatment can be used, and various oils such as vegetable oil and animal oil may be used alone or in combination. .
In the method for producing french fries according to the present invention, various seasonings, sweeteners, nucleic acid-containing nucleic acid seasonings such as amino acids, spices, phosphorus in the aqueous solution of reduced dextrin used for blanching treatment Various additives such as acid salts may be appropriately mixed.
4). EFFECT OF THE INVENTION By producing french fries according to the present invention, it is possible to reduce the content of oil in the french fries contained after oiling and to produce a favorable texture compared to french fries produced by carrying out ordinary blanching treatment It became possible to produce French fries having
5. BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in detail with reference to the following examples, but the technical scope of the present invention is not limited to the following examples. Moreover, in the example shown below, unless otherwise indicated,% shall represent weight%. In addition, commercially available salad oil was used in the oil treatment of the examples and comparative examples.
[Example 1]
Baron candy was used as a raw material for French fries, and after peeling the skin and removing the buds, 300 g was prepared by cutting the length × width × length into a size of approximately 1 cm × 1 cm × 5 to 8 cm.
As a dextrin reductant, a dextrin reductant having a DE of about 8 (trade name: PO-10, manufactured by Towa Kasei Kogyo Co., Ltd.) was used to prepare a dextrin reductant aqueous solution having a solid content of 10.0% by weight. . The content of hydride of sugars having a sugar polymerization degree of 20 or more was 75.0% by weight based on the prepared dextrin reduced solids.
The cut baron jar was added to the boiled dextrin solution and boiled for 3 minutes.
After the blanching treatment, the baron was taken out, drained, allowed to cool to room temperature, and then oiled at 160 to 170 ° C. for 2 minutes as the primary oil. After dipping, the mixture was allowed to cool at room temperature for 10 minutes and stored frozen in a -30 ° C refrigerator for 3 days.
The Baron jar containing the primary oil that had been stored in a frozen state was taken out of the freezer and immediately subjected to a secondary oil squeeze at 180-190 ° C. for 2 minutes to produce Baron potato fries.
[Example 2]
Using North Sea Golden as a raw material for French fries, peeling off the skin and removing the buds, 300 g were prepared in which the length × width × length was cut to a size of approximately 1 cm × 1 cm × 5 to 8 cm.
Using the same dextrin reduced product as in Example 1, a dextrin reduced solution having a solid content of 10.0% by weight was prepared.
The cut North Sea golden was added to the boiled dextrin reductant solution and boiled for 3 minutes.
After the blanching treatment, the baron was taken out, drained, allowed to cool to room temperature, and then oiled at 160 to 170 ° C. for 2 minutes as the primary oil. After dipping, the mixture was allowed to cool at room temperature for 10 minutes and stored frozen in a -30 ° C refrigerator for 3 days.
The frozen North Sea golden fried potato was taken out from the freezer and immediately subjected to secondary oil frying at 180-190 ° C. for 2 minutes to produce North Sea golden french fries.
[Example 3]
A North Sea golden fries was produced in the same manner as in Example 2 except that the solid content of the aqueous dextrin solution used for blanching was 1.0 wt%.
[Example 4]
A North Sea golden fries was produced in the same manner as in Example 2 except that the solid content of the dextrin reductate aqueous solution used for blanching was changed to 5.0% by weight.
[Example 5]
A North Sea golden fries was produced in the same manner as in Example 2 except that the solid content of the dextrin reductate aqueous solution used for blanching was 10.0% by weight.
[Example 6]
A North Sea golden fries was produced in the same manner as in Example 2 except that the solid content of the aqueous dextrin solution used for blanching was 15.0% by weight.
[Example 7]
Using North Sea Golden as a raw material for French fries, peeling off the skin and removing the buds, 300 g were prepared in which the length × width × length was cut to a size of approximately 1 cm × 1 cm × 5 to 8 cm.
Using the same dextrin reduction product as in Example 1, an aqueous dextrin reduction solution having a solid content of 20.0% by weight was prepared.
The cut North Sea golden was immersed in a dextrin reductate aqueous solution adjusted to 25 ° C. for 1 minute.
The North Sea Golden, which was taken out of the immersion liquid and lightly drained, was placed in a steamer previously heated to 100 ° C., and steam blanching was performed for 3 minutes while maintaining the steam temperature at 100 ° C.
After steam blanching, the North Sea golden was taken out and allowed to cool to room temperature, and then oiled at 160-170 ° C. for 2 minutes as the primary oil. After dipping, the mixture was allowed to cool at room temperature for 10 minutes and stored frozen in a -30 ° C refrigerator for 3 days.
The frozen potato-stored primary potatoes were taken out of the freezer and immediately subjected to secondary oil squeezing at 180-190 ° C. for 2 minutes to produce North Sea golden fries.
[Comparative Example 1]
Baron fried potatoes were produced in the same manner as in Example 1 except that no water was added as an aqueous solution used for blanching.
[Comparative Example 2]
As an aqueous solution used for blanching, a dextrin solution having a solid content of 10.0% by weight prepared using a dextrin having a DE of about 8 was used. French fries were produced.
[Comparative Example 3]
As an aqueous solution used for blanching, a reduced starch saccharified aqueous solution having a solid content of 10.0% by weight prepared using a reduced starch saccharified product (trade name: PO-20, manufactured by Towa Kasei Kogyo Co., Ltd.) is used. Baron fried potatoes were produced in the same manner as in Example 1 except that.
The reduced starch saccharified product PO-20 used in this comparative example is a reduced product of starch degradation product having a DE of about 21, and the hydride content of saccharides having a sugar polymerization degree of 20 or more contained per solid is 26. 0.0% by weight.
[Comparative Example 4]
Except for using an aqueous maltitol solution having a solid content of 10.0% by weight prepared using maltitol (trade name: Resis, manufactured by Towa Kasei Kogyo Co., Ltd.) as an aqueous solution used for blanching. Baron fried potatoes were produced in the same manner as in 1.
[Comparative Example 5]
Except for using an aqueous solution of maltose prepared by using maltose (trade name: Sanmart, manufactured by Hayashibara Biochemical Laboratories Co., Ltd.) as the aqueous solution used for blanching, the solid content was 10.0% by weight. Baron fried potatoes were produced in the same manner as in 1.
[Comparative Example 6]
The same as in Example 1 except that a sorbitol aqueous solution having a solid content of 10.0% by weight prepared using sorbitol (trade name: Sorbit, manufactured by Towa Kasei Kogyo Co., Ltd.) was used as an aqueous solution used for blanching. In this way, baron fried potatoes were produced.
[Comparative Example 7]
A North Sea golden french fries was produced in the same manner as in Example 2 except that no water was used as the aqueous solution used for blanching.
[Comparative Example 8]
The same procedure as in Example 2 was used except that a dextrin solution having a solid content of 10.0% by weight was prepared using a dextrin having a DE of about 8 as an aqueous solution used for blanching. French fries were produced.
[Comparative Example 9]
Except for using an aqueous maltitol solution having a solid content of 10.0% by weight prepared using maltitol (trade name: Resis, manufactured by Towa Kasei Kogyo Co., Ltd.) as an aqueous solution used for blanching. In the same way as in No. 2, North Sea golden fries were produced.
[Comparative Example 10]
Except for using an aqueous solution of maltose prepared by using maltose (trade name: Sanmart, manufactured by Hayashibara Biochemical Laboratories Co., Ltd.) as the aqueous solution used for blanching, the solid content was 10.0% by weight. In the same way as in No. 2, North Sea golden fries were produced.
[Comparative Example 11]
A North Sea golden french fries was produced in the same manner as in Example 7 except that water to which nothing was added was used as the aqueous solution used for blanching.
[Comparative Example 12]
In the same manner as in Example 7, except that a dextrin solution having a solid content of 20.0% by weight was prepared using a dextrin having a DE of about 8 as an aqueous solution used for blanching. French fries were produced.
[Comparative Example 13]
As an aqueous solution used for blanching, a reduced starch saccharified aqueous solution having a solid content of 20.0% by weight prepared using a reduced starch saccharified product (trade name: PO-20, manufactured by Towa Kasei Kogyo Co., Ltd.) is used. A North Sea golden french fries was produced in the same manner as in Example 7 except that.
[Comparative Example 14]
Except for using an aqueous solution of maltitol having a solid content of 20.0% by weight prepared using maltitol (trade name: Resis, manufactured by Towa Kasei Kogyo Co., Ltd.) as an aqueous solution used for blanching. In the same manner as in No. 7, North Sea Golden Fried Ote was produced.
[Comparative test 1]
(1) Measurement of oil content in french fries The oil content of the invention product and the comparative product was extracted by the Soxhlet method, and the oil content in the french fries was determined.
The invention and comparative french fries produced in each of the examples and comparative examples were left on a wire mesh for 5 minutes after the end of each oiling, and then oiled and then brought to room temperature on kitchen paper. The sample was allowed to cool until it was removed, and the excess oil exuded from the french fries was removed and ground with a mortar until uniform, and this was used as a sample for measurement.
A sample obtained by randomly collecting about 8 g from the measurement sample was taken as one sample, and 10 samples were collected at random. The collected sample was placed so as not to spill into the cylindrical dry filter paper. The weight of only the dry filter paper at this time was A, and the total weight of the dry filter paper and the sample was B.
With the sample in the dry filter paper, vacuum drying was performed at 60 ° C. for 12 hours, and the total weight of the filter paper and the sample after the drying treatment was weighed.
The sample dried under reduced pressure was subjected to oil extraction for 10 hours in a Soxhlet tube using diethyl ether.
The sample after extraction was dried under reduced pressure at 90 ° C. for 5 hours, the sample weight was measured, and this value was designated as D.
The content of oil in the french fries was determined by weight% based on the total weight of the french fries according to the following calculation formula.
Oil content in french fries (wt%) = (C−D) / (B−A) × 100
[Comparative test 2]
(2) Food texture of french fries The fries according to the present invention were trained using a fried potato produced by branching the crispy feeling on the surface of the fries and the crispy feeling inside the fries with water as a reference product. Relative evaluation by sensory test was conducted on 10 panelists.
About the fried potato which concerns on Example 1 and Comparative Example 1- Comparative Example 6 which used baron potato, the fried potato manufactured by the comparative example 1 was made into the reference | standard product.
For the fries according to Examples 2 to 6 and Comparative Examples 7 to 10 using North Sea gold, the fries manufactured in Comparative Example 7 were used as reference products.
For the fries according to Example 7 and Comparative Examples 11 to 14 using North Sea gold, the fries manufactured in Comparative Example 11 were used as reference products.
The crispness of the surface of the French fries is very good compared to the reference product: ◎, better than the reference product: ○, equivalent to the reference product: △, inferior to the reference product: ×, Many evaluations were the results of sensory tests.
The inside feeling of the French fries is very good compared to the standard product: ◎, better than the standard product: ○, equivalent to the standard product: △, inferior to the standard product: ×, Many evaluations were the results of sensory tests.
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US5928693A (en) * | 1997-11-14 | 1999-07-27 | Cerestar Holding B.V. | Clear coat composition for potato products and method of making |
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