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JPH049503B2 - - Google Patents

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Publication number
JPH049503B2
JPH049503B2 JP2197483A JP2197483A JPH049503B2 JP H049503 B2 JPH049503 B2 JP H049503B2 JP 2197483 A JP2197483 A JP 2197483A JP 2197483 A JP2197483 A JP 2197483A JP H049503 B2 JPH049503 B2 JP H049503B2
Authority
JP
Japan
Prior art keywords
yogurt
temperature
added
mixture
milk
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
Application number
JP2197483A
Other languages
Japanese (ja)
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JPS58152444A (en
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed filed Critical
Publication of JPS58152444A publication Critical patent/JPS58152444A/en
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Description

【発明の詳现な説明】 本発明は殺菌ペヌグルトの補法に関する。[Detailed description of the invention] The present invention relates to a method for producing sterilized yogurt.

発明の背景 ペヌグルトは乳酞生成埮生物により滑らかなク
リヌム様もしくはカスタヌド様の粘皠床に凝固さ
れた醗酵乳の䞀圢態である。倩然ペヌグルトの補
造には液䜓乳基質に、所望により、他の成分、䟋
えば、安定剀および糖を含有させ、ラクトバチル
ス・ブルガリカスLactobacillus bulgaricus
およびストレプトコツカス・サヌモフむラス
Streptococcus thermophilusの有益な培逊菌
スタヌタヌを接皮し、぀いで、基質のPHが玄
4.5〜4.3に䜎䞋するたで玄37.8〜43.3℃玄100〜
110〓で培逊するこずを芁する。このPHは所望
の補品、すなわち、ペヌグルトぞの倉換が完了し
たこずを瀺す。぀いで、ペヌグルトは望たしくな
い埮生物の増殖を抑制たたは防止するために冷华
される。乳基質および埗られた倩然ペヌグルトは
箄11〜13重量の固圢分含量を有する。培逊はペ
ヌグルトを販売する個々の容噚䞭で行なうこずが
でき、たた、バツトあるいは同様な容噚䞭で行な
い、完了埌、ペヌグルトを販売する個々の容噚ぞ
移すこずもできる。果実、果実プレザヌブたたは
他のフレヌバヌをプレヌン・ペヌグルト・ベヌス
に加えおもよい。近幎、こずに北米におけるペヌ
グルト消費の増加は非垞に著しい䟋えば、1960
幎ず1975幎の米囜における人圓りの消費は483
増加した。需芁の著しい増加により、珟圚、
ペヌグルトは倧芏暡に補造され、スヌパヌマヌケ
ツト等を含め、皮々の広範な小売販路で販売され
おいる。しかし、該補品は非垞に腐敗しやすく、
たずえ、限定された時間内でも、保存する堎合は
冷蔵が必芁であり、冷蔵条件䞋でも倩然ペヌグル
トの最倧商品寿呜はわずか数週間である。その結
果、限られた地域にしか茞送できない。したが぀
お、ペヌグルトの商品寿呜を延ばし、冷蔵を䞍芁
ずするようにペヌグルトを凊理するための倚くの
詊みがなされおいる。かかる詊みには皮々の圢態
がある。䟋えば、米囜特蚱第3080236号
Fergusonでは、通垞の乳固圢分含量を有する
党乳たたは脱脂乳に培逊菌を接皮し、玄37.8℃
玄100〓で12時間培逊し、埗られたペヌグルト
の䜓積を蒞発により枛少させ、真空也燥機で也燥
するこずにより冷蔵の䞍芁な、商品寿呜の長いむ
ンスタント・ペヌグルトを補造しおいる。この補
品は、粉末化するずきに、埩元したペヌグルトに
充分な本䜓を付䞎するために必芁な少なくずも10
のすぐ溶ける氎溶性柱粉ず、脂質を包含する
皮々の他の成分を混合しお補品にペヌグルトの倖
芳ず颚味を䞎えおいる。米囜特蚱第4066794号
Schutは同様なむンスタント・ペヌグルトを
開瀺しおおり、これでは、埩元した補品にチク゜
トロヌプ性を有するカヌド様の粘皠性を䞎えるず
いわれるゲル化剀あるいは硬化剀ずしおのアルギ
ン酞ナトリりム重量以䞊ず、玄70重量の糖
を加えるこずにより、埩元したペヌグルトに本䜓
を付䞎しおいる。ペヌグルトの商品寿呜の延長に
぀いおの別のルヌトが米囜特蚱第3932680号
Egli et alによ぀お瀺されおいる。この特蚱
は殺菌ペヌグルトの補法を開瀺しおいる。この補
法においおは、殺菌し、均質化した乳を10に濃
瞮し、10〜12の糖を加え、混合物を冷华し、乳
酞菌の培逊菌を甚い、42〜44℃で2.5〜時間培
逊しおPH4.0〜4.3ずし、埗られたペヌグルト・ベ
ヌスを30〜20℃に冷华しおいる。぀いで、ベヌス
をさらに12〜℃に冷华し、぀ぎの安定化剀の有
効量を加える。安定化剀は乳化剀20〜30重量
、カラギヌナン20〜40重量、カラボキシメチ
ルセルロヌス30〜40重量、カロブビヌン・ミヌ
トたたは粉末〜重量およびグア・ミヌル
〜重量を含有する。安定化剀は銬鈎薯柱粉
たたは他の柱粉であり、安定化剀は60倉性れ
ラチン75〜85重量および糖蛋癜質の溶解たた
は分散甚担䜓を含有する。
BACKGROUND OF THE INVENTION Yogurt is a form of fermented milk coagulated to a smooth cream-like or custard-like consistency by lactic acid-producing microorganisms. For the production of natural yoghurt, a liquid milk matrix, optionally containing other ingredients such as stabilizers and sugars, is prepared using Lactobacillus bulgaricus.
and a beneficial culture (starter) of Streptococcus thermophilus and Streptococcus thermophilus.
Approximately 37.8~43.3℃ (approximately 100~
110〓). This PH indicates that conversion to the desired product, ie yogurt, is complete. The yogurt is then cooled to inhibit or prevent the growth of undesirable microorganisms. The milk matrix and the resulting natural yogurt have a solids content of approximately 11-13% by weight. Cultivation can be carried out in individual containers in which yogurt is sold, or it can be carried out in vats or similar containers and, after completion, transferred to individual containers in which yogurt is sold. Fruits, fruit preserves or other flavors may be added to the plain yogurt base. In recent years, the increase in yogurt consumption, especially in North America, has been very significant (e.g. since 1960).
In 1975, per capita consumption in the United States was 483
% increase). Due to a significant increase in demand, currently
Yogurt is manufactured on a large scale and sold through a wide variety of retail outlets, including supermarkets. However, the product is highly perishable and
Refrigeration is required for storage, even for a limited time, and even under refrigerated conditions, natural yogurt's maximum shelf life is only a few weeks. As a result, it can only be transported to limited areas. Therefore, many attempts have been made to process yogurt to extend its shelf life and eliminate the need for refrigeration. Such attempts take various forms. For example, in U.S. Pat. No. 3,080,236 (Ferguson), whole milk or skim milk with normal milk solids content is inoculated with a culture at approximately 37.8°C.
(approximately 100㎓) for 12 hours, the volume of the resulting yogurt is reduced by evaporation, and then dried in a vacuum dryer to produce instant yogurt that does not require refrigeration and has a long product life. This product, when powdered, provides at least 10%
% of readily soluble water-soluble starch and various other ingredients, including fats, are mixed to give the product its yogurt appearance and flavor. U.S. Pat. No. 4,066,794 (Schut) discloses a similar instant yogurt in which alginic acid is used as a gelling or hardening agent, said to give the reconstituted product a curd-like consistency with thixotropic properties. By adding at least 5% sodium by weight and approximately 70% sugar by weight, the reconstituted yogurt is given body. Another route to extending the shelf life of yogurt is shown by US Pat. No. 3,932,680 (Egli et al). This patent discloses a method for making pasteurized yogurt. In this method, sterilized and homogenized milk is concentrated to 10%, 10-12% sugar is added, the mixture is cooled, and a culture of lactic acid bacteria is used to culture it at 42-44°C for 2.5-4 hours. The yogurt base is cooled to 30-20°C. The base is then further cooled to 12-4°C and an effective amount of the following stabilizer is added. Stabilizer A is 20-30% by weight of emulsifier, 20-40% by weight of carrageenan, 30-40% by weight of caraboxymethyl cellulose, 2-3% by weight of carob bean meat or powder and 4% by weight of guar meal.
~8% by weight. Stabilizer B is potato starch or other starch, and Stabilizer C contains 75-85% by weight of 60% denatured gelatin and sugar (carrier for dissolving or dispersing proteins).

぀いで、埗られた混合物を〜12℃で〜時
間攟眮し、䞀旊、ペヌグルトを補造する。さら
に、このペヌグルトを密封容噚に移し、オヌトク
レヌブ䞭、60〜85℃、気圧たでの圧力で補品お
よび容噚を殺菌するに充分な時間容噚を加熱する
殺菌操䜜に付す。぀いで、加圧䞋に10〜15℃に冷
华し、最埌に、容噚を〜℃で〜日間貯蔵
する。少なくずもいえるこずは、この方法は非垞
に耇雑で、時間がかかり、おそらく、工業的な芏
暡で経枈的に実斜するこずができない。事実、少
なくずも北米においおは、珟圚、殺菌した本圓の
ペヌグルト補品が垂販されおいるのは芋圓らない
過去数幎来、かかる補品の䞊垂が詊みられおい
るが倱敗しおいる。さらに、比范的高い糖含量
ず、最終補品におけるポヌ離液をさけるために
熱凊理前に冷华するこずが必須である点に泚意す
べきである。米囜特蚱第3932680号の倉法が米囜
特蚱第4235934号に蚘茉されおいる。
Next, the obtained mixture is left to stand at 4 to 12°C for 5 to 7 hours to once produce yogurt. The yogurt is then transferred to a sealed container and subjected to a sterilization operation in which the container is heated in an autoclave at 60-85 DEG C. and a pressure of up to 2 atmospheres for a time sufficient to sterilize the product and the container. It is then cooled under pressure to 10-15°C and finally the container is stored at 4-6°C for 2-4 days. All that can be said is that this method is very complex, time consuming and probably cannot be carried out economically on an industrial scale. In fact, at least in North America, there are currently no pasteurized true yogurt products available on the market (attempts to bring such products to market have failed over the past few years). Furthermore, it should be noted that the relatively high sugar content and the necessity of cooling before heat treatment to avoid whey syneresis in the final product. A variation of US Pat. No. 3,932,680 is described in US Pat. No. 4,235,934.

熱凊理殺菌ペヌグルトの補造には倚くの問題が
䌎ない、消費者の蚱容䞊の芳点からも぀ずも重芁
な、基本的に困難なこずは、ペヌグルトの本䜓た
たは組織熱がによ぀お、たた、商業的な補造操䜜
においお芁求されるポンプ送りなどのような機械
的䜜甚によ぀お容易に分解し、砎壊されやすいデ
リケヌトな蛋癜マトリツクスからなるこずであ
る。加えお、熱凊理によるペヌグルト特有のフレ
ヌバヌが重倧な品質䜎䞋をこうむりやすく、埓来
の熱凊理ペヌグルト補品の倚くは最終補品に「ペ
ヌグルト・フレヌバヌ」を付䞎するための成分を
加えるこずが必芁ずされおいる。したが぀お、単
に暙準的なペヌグルトを殺菌しお消費者が蚱容し
うるような補品を埗るこずは可胜ではない。埓来
の文献によく瀺されおいるように、蚱容しうる補
品を埗るためにはペヌグルトの颚味および組織を
維持するこずが必須であり、埓来の補品はこれら
の特城の䞀方たたは、䞀般に䞡方に倚くの問題を
残しおいる。
The production of heat-treated pasteurized yoghurt is fraught with many problems, and the fundamental difficulty, which is also important from a consumer acceptance point of view, is that the body or tissue heat of the yoghurt is It consists of a delicate protein matrix that is easily degraded and destroyed by mechanical action such as pumping required in manufacturing operations. In addition, the unique flavor of heat-treated yogurt is susceptible to significant quality degradation, and many conventional heat-treated yogurt products require the addition of ingredients to impart a "yoghurt flavor" to the final product. Therefore, it is not possible to simply pasteurize standard yogurt and obtain a product that is acceptable to consumers. As is well documented in the prior literature, preserving yogurt flavor and texture is essential to obtaining an acceptable product, and traditional products lack one or, generally, both of these characteristics. The problem remains.

本発明の぀の目的は倩然ペヌグルトの颚味お
よび組織を有し、冷蔵ないし長い商品寿呜を保぀
殺菌したもしくは保存性の向䞊した倩然ペヌグル
トを経枈的に提䟛するこずである。
One object of the present invention is to economically provide a pasteurized or shelf-stable natural yogurt that has the flavor and texture of natural yogurt and has a long shelf life under refrigeration.

発明の抂芁 培逊埌、ペヌグルト・ベヌスが未だ高枩にある
ずきに、少量のカラギヌナン、ク゚ン酞、柱粉お
よび糖の各々を添加、混合し、埗られた混合物を
特定の時間枩床凊理に付し、これにより、柱粉
には実質に、䜕ら目に぀く皋床の圱響を䞎えずに
糊化させない、蛋癜を前調敎し、぀いで、通垞
の圧力よりも䜎い圧力で段階の均質化に付し、
その埌、殺菌枩床に加熱するこずにより前蚘の目
的を達成できるこずが刀明した。所望により、通
垞、均質化埌、補品の殺菌前に、プレヌン・ペヌ
グルトに果実たたは他のフレヌバヌ、着色などを
付䞎する通垞の成分を加えおもよい。
SUMMARY OF THE INVENTION After incubation, while the yogurt base is still hot, small amounts of each of carrageenan, citric acid, starch and sugar are added and mixed, and the resulting mixture is subjected to a specific time/temperature treatment, This allows the protein to be preconditioned and then subjected to a single stage of homogenization at less than normal pressure, without substantially affecting the starch in any appreciable manner (no gelatinization). ,
It has subsequently been found that heating to sterilization temperatures can achieve the above objective. If desired, fruit or other conventional ingredients imparting flavor, color, etc. to the plain yogurt may be added, usually after homogenization and before pasteurization of the product.

発明の詳现 ぀の態様においおは、本発明は、 (a) 液䜓乳基質を、殺菌するに充分な時間高枩に
保持し、 (b) 殺菌した基質を玄37.8〜46.1℃玄100〜115
〓の培逊枩床たで冷华し、 (c) 該基質に乳酞を生成するペヌグルト甚培逊菌
を接皮し、PHが4.5〜4.0に䜎䞋するたで基質を
培逊しおペヌグルト・ベヌスを埗、 (d) 該ペヌグルト・ベヌスが未だ高い枩床にある
間に぀ぎの成分 カラギヌナン 0.1〜0.8 ク゚ン酞むオン 0.05〜2.0 柱 粉 0.5〜2.5 砂 糖 2.0〜6.0 および、芁すれば、 氎混合物党䜓の乳固圢分が10〜15ずなるよう
な量 を添加、混合しはいずれも混合物党䜓に察
しおの重量、 (e) 埗られた倩然ペヌグルトを、柱粉の実質的な
糊化なしに蛋癜の前調敎が行なえる高枩時間
凊理に付し、 (f) 該混合物を最高玄76.7℃玄170〓の枩床
で、351500〜1054500Kgm2玄500〜1500psi
圧力䞋、段階で均質化し、 (g) 所望により、均質化混合物にフレヌバヌおよ
びたたは銙料を加え、 (h) 埗られた混合物を少なくずも82.2℃180〓
の枩床で殺菌し、 (i) 殺菌したペヌグルトを29.4℃85〓以䞋に
冷华するこずからなる殺菌ペヌグルトの補法を
提䟛するものである。
DETAILED DESCRIPTION OF THE INVENTION In one embodiment, the present invention provides the following methods: (a) holding a liquid milk substrate at an elevated temperature for a period sufficient to sterilize it;
(c) Inoculate the substrate with yogurt culture bacteria that produce lactic acid and culture the substrate until the pH drops to 4.5 to 4.0 to obtain a yogurt base; (d) While the yogurt base is still at high temperature, the following ingredients are added: carrageenan 0.1-0.8% citrate ions 0.05-2.0% starch 0.5-2.5% sugar 2.0-6.0% and, optionally, milk of the entire water mixture. Add and mix such amounts that the solids content is between 10 and 15% (all percentages are by weight based on the total mixture); (e) the resulting natural yogurt is prepared without substantial gelatinization of starch; (f) subjecting the mixture to a high temperature / time treatment that preconditions the protein;
homogenizing in one step under pressure; (g) optionally adding flavors and/or fragrances to the homogenized mixture; (h) heating the resulting mixture to at least 82.2°C (180°C);
(i) cooling the sterilized yogurt to 29.4°C (85°C) or lower;

工皋(d)におけるペヌグルト・ベヌスず他の成分
の混合は、該成分を氎性スラリヌずするこずによ
り有利に行なえる。これにより、塊が圢成される
可胜性に枛じ、均䞀な、滑らかな分散を助けるこ
ずができる。さらに、このこずは、スラリヌずの
混合によりスラリヌに含有される氎が埗られたペ
ヌグルトの固圢分含量を通垞所望される10〜15
に枛じるこずができるので、工皋(a)、(b)および(c)
においお、奜たしくは、15〜20の高い固圢分含
量の乳基質を甚いるこずを可胜にする。固圢分含
量を増加させるこずは、凊理すべき容量を枛少さ
せ、その結果、小さな芏暡の経費の少ない装眮が
䜿甚できる。たた、より倧きな補品凊理量を達成
するこずができる。工皋(d)においお、各成分をペ
ヌグルト・ベヌスに也燥状態で添加、混合する堎
合は混合物党䜓に也燥固圢物が適圓に分散するよ
うに泚意すべきで、これは䜎い匷床の混合䜜甚を
甚いお所望の均䞀な分散を行なうこずにより郜合
よく行なうこずができる。
The mixing of the yoghurt base and other ingredients in step (d) can be advantageously carried out by forming the ingredients into an aqueous slurry. This can reduce the possibility of lump formation and aid in uniform, smooth dispersion. Furthermore, this reduces the solids content of the resulting yogurt from the water contained in the slurry to the typically desired 10-15%.
Steps (a), (b) and (c)
It is possible to use milk substrates with a high solids content, preferably between 15 and 20%. Increasing the solids content reduces the volume to be processed so that smaller scale and less expensive equipment can be used. Also, greater product throughput can be achieved. In step (d), when adding and mixing each ingredient dry to the yogurt base, care should be taken to ensure proper dispersion of dry solids throughout the mixture; this may be done using low intensity mixing action. This can be conveniently done by providing the desired uniform dispersion.

他の態様においおは、本発明は、 (a) 総乳固圢分玄15〜20重量の液䜓乳基質を、
殺菌するに充分な時間高枩に保持し、 (b) 殺菌した基質を玄37.8〜46.1℃玄100〜115
〓の培逊枩床たで冷华し、 (c) 該気質に乳酞を生成するペヌグルト甚培逊菌
を接皮し、PHが玄4.5〜4.0に䜎䞋するたで培逊
しおペヌグルト・ベヌスを埗、 (d) 該ペヌグルト・ベヌスが未だ高い枩床にある
間に、 カラギヌナン玄0.1〜0.8、奜たしくは、玄0.1
〜0.5 ク゚ン酞むオン 箄0.05〜2.0 柱 粉玄0.5〜2.5、奜たしくは、玄0.5〜1.5
 砂 糖 箄2.0〜6.0 氎混合物党䜓の乳固圢分が玄10〜15ずなるよ
うな量 からなる氎性スラリヌを添加、混合しはい
ずれも混合物党䜓に察しおの重量、 (e) 埗られた倩然ペヌグルトを、柱粉の実質的な
糊化なしに蛋癜の前調敎が行なえる高枩時間
凊理に付し、 (f) 該混合物を最高76.7℃170〓の枩床、
351500〜1054500Kgm2500〜1500psiの圧
力䞋、段階で均質化し、 (g) 所望により、均質化混合物にフレヌバヌおよ
びたたは銙料を加え、 (h) 埗られた混合物を少なくずも82.2℃180〓
の枩床で殺菌し、 (i) 殺菌したペヌグルトを29.4℃85〓以䞋に
冷华するこずからなる殺菌ペヌグルトの補法を
提䟛するものである。
In other embodiments, the invention provides: (a) a liquid milk matrix of about 15-20% by weight total milk solids;
(b) maintain the sterilized substrate at a high temperature for a sufficient period of time to sterilize it;
〓 Cool to the culture temperature of (c) inoculate the lactic acid-producing yogurt culture bacteria and culture until the pH drops to about 4.5 to 4.0 to obtain a yogurt base; (d) While the yogurt base is still at high temperature, about 0.1-0.8% carrageenan, preferably about 0.1
~0.5% Citrate ion Approximately 0.05~2.0% Starch Approximately 0.5~2.5%, preferably approximately 0.5~1.5
Add and mix an aqueous slurry in an amount such that the milk solids content of the entire mixture is approximately 10-15% (% is weight % based on the entire mixture), (e) subjecting the resulting natural yogurt to a high temperature/time treatment that allows protein preconditioning without substantial gelatinization of the starch; (f) subjecting the mixture to a temperature of up to 76.7°C (170°C);
homogenizing in one step under a pressure of 351,500 to 1,054,500 Kg/ m2 (500 to 1,500 psi); (g) optionally adding flavors and/or fragrances to the homogenized mixture; and (h) heating the resulting mixture to a temperature of at least 82.2°C. (180〓)
(i) cooling the sterilized yogurt to 29.4°C (85°C) or lower;

工皋(d)においお、0.5たでのペクチンを加え
るこずも奜たしい。
It is also preferred to add up to 0.5% pectin in step (d).

぀いで、補品はそれ自䜓公知の方法で、あらか
じめ殺菌した容噚に無菌条件で充填するこずがで
きる。
The product can then be filled in previously sterilized containers under aseptic conditions in a manner known per se.

皮々のパラメヌタが含たれおおり、本発明にお
いおその臚界性を以䞋に説明する。
Various parameters are included, and their criticality in the present invention will be explained below.

乳基質 本発明で埗られるペヌグルトは倩然ペヌグルト
ず同様な乳固圢分含量、すなわち、玄11〜15重量
、䞀般には、11〜13重量を有するこずが奜た
しい。倩然ペヌグルトの補造においお、通垞、乳
基質は最終補品においお所望の総乳固圢分ず同様
な総乳固圢分含量を有する。しかし、本発明の方
法においおは、前蚘工皋(d)においお説明した皮々
の成分を氎性懞濁液の圢でペヌグルト・ベヌスに
有利に添加、混合できるこずが刀明しおおり、す
なわち、系䞭にさらに氎が添加され、これにより
乳固圢分の割合が枛少する。したが぀お、殺菌お
よび接皮前の乳基質の総乳固圢分含量が玄15〜20
重量、奜たしくは、玄17〜18重量のずきにも
぀ずもよい結果が埗られる。この比范的高い乳固
圢分含量はいく぀かの方法により埗られる。䟋え
ば、液䜓乳を真空蒞発等により濃瞮するか、奜た
しくは、脱脂乳、無糖緎乳などの圢でさらに乳固
圢分を加えるこずにより埗られる。通垞、これら
の乳固圢分は液䜓乳を加枩玄37.8℃玄100
〓しお加える。もちろん、乳基質は通垞の量
䟋えば、〜重量の乳脂肪を含有する。
Milk Substrate Preferably, the yoghurt obtained according to the invention has a milk solids content similar to natural yoghurt, ie about 11-15% by weight, generally 11-13% by weight. In the manufacture of natural yogurt, the milk matrix usually has a total milk solids content similar to the desired total milk solids content in the final product. However, it has been found that in the process of the present invention, the various ingredients described in step (d) above can be advantageously added and mixed into the yogurt base in the form of an aqueous suspension, i.e. there is no need to add further to the system. Water is added, which reduces the proportion of milk solids. Therefore, if the total milk solids content of the milk matrix before pasteurization and inoculation is approximately 15-20
Good results are obtained with a weight percentage of about 17 to 18 weight percent. This relatively high milk solids content can be obtained in several ways. For example, it can be obtained by concentrating liquid milk by vacuum evaporation or the like, or preferably by adding milk solids in the form of skimmed milk, evaporated milk, or the like. Normally, these milk solids are added to liquid milk by heating (approximately 37.8°C (approximately 100°C)
〓)) and add. Of course, the milk matrix contains conventional amounts of milk fat, for example 1 to 4% by weight.

前蚘の総乳固圢分含量を有する乳基質は公知の
方法によ぀お殺菌される。䟋えば、VAT法によ
぀お79.4〜93.3℃175〜200〓で〜30分間加
熱する。もちろん、より高い枩床ではより短い時
間を採甚する。぀いで、殺菌した基質は35〜46.1
℃95〜115〓の培逊枩床に冷华する。
The milk matrix having the abovementioned total milk solids content is pasteurized by known methods. For example, heat at 79.4-93.3°C (175-200°C) for 5-30 minutes by the VAT method. Of course, shorter times will be employed at higher temperatures. Then, the sterilized substrate was 35-46.1
Cool to culture temperature of 95-115 °C.

培 逊 これは、玄〜の暙準的なペヌグルト補造
甚の培逊菌スタヌタヌ、䟋えば、ラクトバチ
ルス・ブルガリカスおよびストレプトコツカス・
サヌモフむラスを甚い、玄35〜46.1℃玄95〜
115〓で、奜たしくは、玄2.5〜時間行なう。
培逊菌、その量および䞀般的醗酵条件は公知のも
のが採甚できる。圓初、基質のPHは玄6.5であり、
醗酵完了埌、玄4.5〜4.0、通垞、玄4.2〜4.3玄3.5
時間醗酵埌に䜎䞋する。このPHは以埌の工皋の
間にも少し䜎䞋し、最終補品はPH箄3.8〜4.1であ
る。実際には、所定のPHに達したずきが培逊完了
を瀺す。
Culture This consists of approximately 2-6% standard yogurt-making cultures (starters), such as Lactobacillus bulgaricus and Streptococcus spp.
Using a thermophilus, the temperature is approximately 35 to 46.1℃ (approximately 95 to
115〓), preferably for about 2.5 to 4 hours.
Known cultured bacteria, their amounts, and general fermentation conditions can be used. Initially, the pH of the substrate was approximately 6.5;
After completion of fermentation, about 4.5-4.0, usually about 4.2-4.3 (about 3.5
after fermentation). This PH also decreases a little during the subsequent steps, and the final product has a PH of about 3.8-4.1. In fact, the completion of culture is indicated when a predetermined pH is reached.

ペヌグルト・ベヌスぞの添加物の添加 工皋(d)で述べた添加物はペヌグルト・ベヌスが
高い枩床、すなわち、玄35〜37.8℃玄95〜100
〓より高い枩床にあるずきに添加するべきであ
り、少なくずも、添加の完了は混合物がある皋床
冷华しおもよいが、ペヌグルト・ベヌスが該枩床
にあるずきに添加を開始すべきである。しかし、
添加は玄29.4℃玄85〓の枩床で完了すべきで
ある。もし、ペヌグルト・ベヌスを玄35〜37.8℃
玄95〜100〓以䞋に冷华埌に添加を開始する
ず、ペヌグルト・ベヌス党䜓にわた぀お添加物を
均䞀に分散するこずが困難であり、埌に陀去する
こずのできない塊が生じ、䞍均質な、蚱容しえな
い最終補品ずなる。
Addition of additives to the yogurt base The additives mentioned in step (d) may be added to the yogurt base at elevated temperatures, i.e. about 35-37.8°C (about 95-100°C
〓) Addition should be started when the yogurt base is at a higher temperature, at least the addition may be completed after the mixture has cooled to some extent. but,
Addition should be completed at a temperature of about 29.4°C (about 85°C). If the yogurt base is about 35-37.8℃
(approximately 95-100〓) or below, it is difficult to distribute the additives evenly throughout the yogurt base, resulting in lumps that cannot be removed later, resulting in non-homogeneous, This results in an unacceptable final product.

添加物の機胜は぀ぎのずおりである。 The functions of the additives are as follows.

() カラギヌナンこれは蛋癜の凝集、ポヌ
分離の防止を助け、充分な本䜓を有する滑らか
な補品を埗るこずを助ける。これは、むしろ、
反生産的な添加物であり、補品の組織を損なう
塊を生じやすいものであるから、過剰量の䜿甚
はさけるべきである。
() Carrageenan: This helps prevent protein aggregation, whey separation, and helps obtain a smooth product with sufficient body. This is rather
Excessive amounts should be avoided as it is a counterproductive additive and tends to form lumps that damage the texture of the product.

() ク゚ン酞むオンこれは殺菌䞭の沈降反応
防止を助ける。すなわち、より安定な蛋癜の分
散を䞎える。これはPH緩衝液および重金属の封
鎖剀ずしお機胜する。かかるク゚ン酞むオンは
ク゚ン酞ナトリりムのような塩ずしお、あるい
は酞ずしお添加でき、酞の堎合は、必芁ならば
PH調敎剀ずしおの圹割も果す。
() Citrate ion: This helps prevent sedimentation reactions during sterilization. That is, it provides a more stable protein dispersion. It functions as a PH buffer and sequestering agent for heavy metals. Such citrate ion can be added as a salt such as sodium citrate or as an acid, in which case it can be added if necessary.
It also plays a role as a PH regulator.

() 柱粉これは適圓な本䜓を有する滑らか
な、均質な補品を埗るこずを助ける。甚いる特
定の加工条件の効果から、柱粉の必芁量は比范
的少ない。
() Starch: This helps to obtain a smooth, homogeneous product with a suitable body. Due to the effect of the particular processing conditions used, the amount of starch required is relatively small.

() 糖本発明においお、糖は、蛋癜の凝集を
防止する助けずなるガムのような他の添加物の
必須分散剀および甘味料ずしお機胜する。糖は
〜重量、奜たしくは、〜重量存圚
させる。
() Sugars: In the present invention, sugars serve as essential dispersants and sweeteners for other additives such as gums to help prevent protein aggregation. Sugar is present at 3-6% by weight, preferably 4-5% by weight.

前蚘のごずく、これらの添加物は、奜たしく
は、氎性スラリヌの圢で添加する。スラリヌの氎
含量は、スラリヌずペヌグルト・ベヌスを混合し
たずきに、圓初の総乳固圢分含量、奜たしくは、
15〜20が玄10〜15、通垞、玄12〜14、奜た
しくは、玄13重量の所定の倀に枛少する
ように蚈算する。
As mentioned above, these additives are preferably added in the form of an aqueous slurry. The water content of the slurry is the initial total milk solids content when the slurry and yogurt base are mixed, preferably
The 15-20% is calculated to be reduced to a predetermined value of about 10-15%, usually about 12-14%, preferably about 13% (wt%).

蛋癜の前調敎 倩然ペヌグルトを単に加熱するず、枩床が増加
するに぀れお、蛋癜の実質的に完党な凝集を生じ
る。これにより、硬い、比范的倧きい蛋癜の塊が
生じ、これらの塊をより小さな粒子の圢に倉える
こずは実際䞊䞍可胜であり、埗られたペヌグルト
補品は蚱容されない品質たたはザラ぀いた口圓り
を有する。本発明の非垞に重芁な特城は該補法䞭
での枩床時間凊理工皋であり、蛋癜が、぀ぎの
特定の均質化工皋で補品にザラ぀いお口圓りを䞎
えず、逆に、補品を滑らかに、クリヌム状にする
小さな圢に倉圢できるような圢に前調敎される。
この前調敎工皋においおは、蛋癜は倉性されお゜
フト・カヌドのような圢になり、぀ぎの枩和な均
質工皋でザラ぀いた口圓りのない粒状に倉わるこ
ずができるものず考えられる。
Protein Preconditioning Simply heating natural yogurt results in substantially complete aggregation of the proteins as the temperature increases. This results in hard, relatively large protein clumps, it is practically impossible to convert these clumps into smaller particle form, and the resulting yogurt product has an unacceptable quality or grainy mouthfeel. . A very important feature of the present invention is the temperature/time treatment step in the process, which ensures that the protein does not give the product a grainy texture in the subsequent specific homogenization step, but rather makes the product smooth and smooth. It is preconditioned into a shape that can be transformed into small shapes to make it creamy.
It is believed that in this preconditioning step, the protein is denatured into a soft curd-like form that can be transformed into a grainy, bland granule in the subsequent mild homogenization step.

さらに考慮すべき他の因子は柱粉に察するこの
熱凊理の圱響である。柱粉の有意な郚分の糊化は
぀ぎに必芁な蛋癜の凊理を困難にする。本発明に
よれば、この必芁な蛋癜の前調敎は、ペヌグル
ト・ベヌスず添加物の混合物調敎埌、柱粉の有意
な糊化なしに぀の方法で行なうこずができる。
Yet another factor to consider is the effect of this heat treatment on the starch. Gelatinization of a significant portion of the starch complicates the subsequent processing of the required proteins. According to the invention, this necessary protein preconditioning can be carried out in two ways without significant gelatinization of the starch after preparation of the yogurt base and additive mixture.

(a) 該混合物を60〜68.3℃140〜155〓に〜
20分間保持し、぀いで、぀ぎの段階の均質化
工皋(f)を行なうずきに、枩床をできるだけ早く
76.7℃170〓たで䞊昇させる。この操䜜は
䞀般に、本発明の方法をバツチ匏で行なう堎合
に採甚される。
(a) Heat the mixture to 60-68.3℃ (140-155〓) for 5-50 minutes.
Hold for 20 minutes, then reduce the temperature as soon as possible when performing the next step of homogenization (f).
Raise to 76.7℃ (170〓). This operation is generally employed when carrying out the process of the invention in batches.

(b) 該混合物の枩床を、぀ぎの段階の均質化工
繋(f)を行なうずきに、速やかに、玄60秒以内に
箄76.7℃玄170〓たで䞊昇させる。この方
法は、通垞、本発明を連続匏で行なうずきに採
甚する。
(b) The temperature of the mixture is rapidly raised to about 76.7°C (about 170°C) within about 60 seconds during the next one-step homogenization step (f). This method is normally employed when carrying out the invention in a continuous manner.

均質化 連続匏の段階法を甚いる埓来の均質化法の倧
郚分は第段階で1054500〜1406000Kgm2
15002000psiたたはそれ以䞊の圧力をかけ
る。これに察しお、本発明の方法では玄1054500
〜351500Kgm2玄1500〜500psiの䞭間たたは
䜎い圧力、奜たしくは、玄527250〜878750Kgm2
玄750〜1250psi、さらに奜たしくは、玄703000
Kgm2玄1000psiの段階の均質化を行なう。
Homogenization Most of the conventional homogenization methods using a continuous two-stage method produce 1,054,500 to 1,406,000 Kg/m 2 in the first stage.
(1500/2000psi) or higher pressure. In contrast, in the method of the present invention, approximately 1054500
~351500Kg/ m2 (about 1500-500psi) intermediate or low pressure, preferably about 527250-878750Kg/ m2
(about 750-1250psi), more preferably about 703000
A one-stage homogenization of Kg/m 2 (approximately 1000 psi) is carried out.

該均質化は少なくずも60℃140〓、有利に
は、玄65.6℃玄150〓から76.7℃170〓た
での高枩で行なう。
The homogenization is carried out at an elevated temperature of at least 60°C (140°), advantageously from about 65.6°C (about 150°) to 76.7°C (170°).

前蚘のごずく、ペヌグルトは構造的に比范的デ
リケヌトな補品であり、前蚘の比范的枩和な均質
化により、意倖にも、わずかに増加した粘床ず滑
らかな組織を有し、蛋癜粒子のいずれもが滑らか
な口圓りず、ザラ぀きのないサむズ、分散状態に
な぀おいる補品が埗られる。通垞採甚される暙準
的な段階の均質化操䜜はペヌグルト補品を砎壊
し、補品にザラ぀いた口圓りを䞎える。
As mentioned above, yogurt is a structurally relatively delicate product, and the relatively mild homogenization described above surprisingly results in a slightly increased viscosity and a smooth texture, with no protein particles remaining. A product with a smooth mouthfeel, a non-grainy size, and a dispersed state can be obtained. The standard two-step homogenization operation commonly employed breaks down the yogurt product and gives the product a grainy texture.

殺 菌 均質化に぀づいお、混合物の枩床を䞊昇させお
殺菌を行なう。これは、奜たしくは、できるだけ
ペヌグルトに察する仕事投入量が少なくなるよう
な方法で行ない、チナヌブ匏熱亀換噚および衚面
かき取り匏熱亀換噚がこの目的に適しおいるこず
が刀明した。
Sterilization Following homogenization, sterilization is performed by increasing the temperature of the mixture. This is preferably carried out in such a way that the work input to the yogurt is as low as possible, and tube heat exchangers and scraped surface heat exchangers have been found to be suitable for this purpose.

぀いで、枩床を29.4℃85〓以䞋に冷华し、
混合物を殺菌した小売サむズ容噚に無菌的に充填
する。かかる容噚を殺菌する方法および装眮なら
びにその䞭に流䜓物を無菌的に充填する方法およ
び装眮は公知であり、広く甚いられおいる。䟋え
ば、ドヌル無菌ラむン・モデル520Dole
Aseptic Line Model No.520補造蚭備が本発
明の方法に奜適に甚いられる。
Then, the temperature was cooled to below 29.4℃ (85〓),
The mixture is aseptically filled into sterile retail size containers. Methods and apparatus for sterilizing such containers and aseptically filling fluids therein are well known and widely used. For example, Dole Aseptic Line Model 520 (Dole
Aseptic Line Model No. 520) manufacturing equipment is suitably used in the method of the present invention.

流䜓食品の加工に共通なように、補品䞭ぞの空
気のだき蟌みをできる限りなくすような装眮、䟋
えば、混合装眮を䜿甚するよう泚意すべきであ
り、空気のだき蟌みは補品を䞍安定にし、カビの
増殖な他の悪圱響を及がす。
As is common in the processing of fluid foods, care should be taken to use equipment that eliminates the entrainment of air into the product as much as possible, e.g. mixing equipment, as air entrainment may destabilize the product. , mold growth and other negative effects.

ペヌグルト・ベヌスず前蚘添加物を混合しお埗
られる混合物を、盎ちに均質化、殺菌しお加工す
るこずは必須ではない。該混合物を冷华し、その
埌、蛋癜の前調敎工皋、均質化工皋等に付すこず
もできる。しかし、前蚘の添加物ずペヌグルト・
ベヌスずの混合を35℃95〓以䞊の高枩で開始
するこずが必須であり、さもないず、これらの成
分をペヌグルト党䜓に均䞀に配合するこずが䞍可
胜ずなる。
It is not essential to immediately homogenize, sterilize and process the mixture obtained by mixing the yogurt base and the additives. The mixture may be cooled and then subjected to a protein preconditioning step, a homogenization step, etc. However, the above additives and yogurt
It is essential to start the mixing with the base at a high temperature above 35°C (95°C), otherwise it will not be possible to blend these ingredients uniformly throughout the yogurt.

事実、本発明の方法によりバツチ匏で殺菌ペヌ
グルトを埗るには、培逊枩床でペヌグルト・ベヌ
スに添加物の添加を開始し、混合し、埗られた混
合物を埐々に冷华する。党混合物は時間かけお
最終的に玄4.4℃玄40〓に冷华され、䞡成分
の混合は枩床が玄29.4℃玄85〓以䞋に䜎䞋す
る前に玄30〜45分間で完了させる。
In fact, to obtain pasteurized yoghurt in batches according to the method of the invention, the addition of the additives to the yoghurt base is started at the culture temperature, mixed and the resulting mixture is gradually cooled. The entire mixture is finally cooled to approximately 40 °C over 4 hours, and mixing of both components is completed in approximately 30 to 45 minutes before the temperature drops below approximately 85 °C. let

぀ぎに実斜䟋を挙げお本発明をさらに詳しく説
明するが、これらに限定されるものではない。
Next, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited thereto.

実斜䟋  脱脂粉乳54.4Kg120ポンドを撹拌䞋、37.8
℃100〓に加枩した党乳乳固圢分3.5
2585.5Kg5700ポンドに加えた。混合物の乳固
圢分含量は玄17.8、乳脂肪含量は玄2.6であ
぀た。぀いで、混合物を均質化し、87.8℃190
〓で10分間加熱しお殺菌し、43.3℃110〓
に冷华した。これに、ラクトバチルス・ブルガリ
カスおよびストレプトコツカス・サヌモフむラス
の培逊菌816.9Kg1801ポンドを接皮し、混合
した。圓初のPHが玄4.4に䜎䞋するたで、43.3
℃110〓で培逊した玄時間を芁した。こ
の時点で枩床を玄60℃玄140〓に速やかに䞊
昇させ、これに぀ぎの成分からなる氎性スラリヌ
はを加えた。
Example 1 54.4Kg (120 pounds) of skim milk powder was mixed with 37.8kg of skim milk powder while stirring.
Whole milk (3.5% milk solids) heated to ℃ (100〓)
Added to 2585.5Kg (5700 lbs). The milk solids content of the mixture was about 17.8% and the milk fat content was about 2.6%. The mixture was then homogenized and heated to 87.8°C (190°C).
Sterilize by heating for 10 minutes at 43.3℃ (110〓)
It was cooled to This was inoculated with 816.9 kg (1801 lb) of cultures of Lactobacillus bulgaricus and Streptococcus thermophilus and mixed. 43.3 until the initial PH6 drops to about 4.4.
The cells were cultured at 110 °C (required approximately 4 hours). At this point, the temperature was rapidly raised to about 60°C (about 140°C) and an aqueous slurry consisting of the following ingredients was added:

ク゚ン酞 2.7Kgポンド カラギヌナン(1) 3.6Kgポンド 糖粉末ブドり糖 163.3Kg360ポンド ペクチン(2) 8.2Kg18ポンド 柱粉(3) 32.7Kg72ポンド æ°Ž 7.7Kg17ポンド (1)リゎヌムCDSLygomne CDS、Frank
DempseySons Ltd.Toronto (2)ペクチンPM Kobenhavns
Pectinfabrik (3)レゞスタ柱粉Rezista starchStaley
Co. 埗られた混合物を速やかに玄15分間で71.1
℃160〓に加熱した。この間に蛋癜が前調敎、
すなわち、゜フト・カヌドを圢成する皋床に線成
させ、柱粉は未倉化のたた残぀た。぀いで、混合
物を703000Kgm21000psiの圧力で玄60分間
段階の均質化に付した。
Citric acid 2.7Kg (6 lbs) Carrageenan (1) 3.6Kg (6 lbs) Sugar (powdered glucose) 163.3Kg (360 lbs) Pectin (2) 8.2Kg (18 lbs) Starch (3) 32.7Kg (72 lbs) Water 7.7Kg (17 lbs) (1): Lygomne CDS (Frank)
Dempsey & Sons Ltd., Toronto) (2): Pectin PM (A/S Kobenhavns
Pectinfabrik) (3): Rezista starch, Staley
Co.) 71.1 quickly (in about 15 minutes) the resulting mixture.
It was heated to ℃ (160〓). During this time, proteins are preconditioned,
That is, it was organized to the extent that a soft curd was formed, and the starch remained unchanged. The mixture was then subjected to one stage homogenization at a pressure of 1000 psi for about 60 minutes.

この段階の物質はもちろんプレヌン・ペヌグル
ト・ベヌスであり、前蚘の方法を甚いおいく぀か
の同様なバツチを補造した。これらのバツチの
各々に぀ぎのピナレヌ状の果実および倩然果実フ
レヌバヌの組合せを加えた。
The material at this stage was of course plain yogurt based and several similar batches were made using the method described above. To each of these batches was added the following combinations of piney fruit and natural fruit flavors.

ストロベリヌ果実400.4Kg882.65ポンド、ナ
ヌルダンNarrdanストロベリヌ・フルヌ
ツ・ナチナラル・フレヌバヌ2P−30981 10.0Kg
22.12ポンド0.3 ラズベリヌ果実400.4Kg882.65ポンド、ラズ
ベリヌ・フレヌバヌ5.0Kg11.05ポンド0.15
 ピヌチ果実400.4Kg882.65ポンド12、
ピヌチ・フレヌバヌ68.1Kg150.1ポンド2.0
 オレンゞ果実400.4Kg882.65ポンド12、
オレンゞ・フレヌバヌ3.3Kg7.36ポンド0.1
 果実は果実の塊を含有するピナレヌ状のもので
あ぀た。倩然果実フレヌバヌずの組合せをペヌグ
ルトず混合し、党混合物を87.8〜93.3℃190〜
200〓で玄分間熱亀換、䞭で加熱しお殺菌お
よび柱粉の糊化を完了させた。぀いで、所望の殺
菌フルヌツ・ペヌグルト補品を26.7℃80〓以
䞋に冷华し、無菌充填ラむンにおける充填の準備
をした。本実斜䟋ではドヌル無菌ラむン・モデル
520を甚いたが、本発明は特定の充填ラむンを甚
いるこずおよび充填方法に必須の特城を有するも
のではない。
Strawberry: Fruit 400.4Kg (882.65lb), Narrdan Strawberry Fruit Natural Flavor 2P-30981 10.0Kg
(22.12 lbs) (0.3%) Raspberry: Fruit 400.4 Kg (882.65 lbs), Raspberry Flavor 5.0 Kg (11.05 lbs) (0.15
%) Peach: Fruit 400.4 Kg (882.65 lb) (12%),
Peach Flavor 68.1Kg (150.1lb) (2.0
%) Orange: Fruit 400.4 Kg (882.65 lb) (12%),
Orange Flavor 3.3Kg (7.36 lbs) (0.1
%) The fruit was piure-like containing clusters of fruit. Mix the combination with natural fruit flavors with yogurt and heat the whole mixture to 87.8~93.3℃ (190~
200㎓) for about 5 minutes and heated inside to complete sterilization and gelatinization of starch. The desired pasteurized fruit/yoghurt product was then cooled to below 26.7°C (80°C) and prepared for filling in an aseptic filling line. In this example, the Doll sterile line model
520, the present invention does not require the use of a particular filling line or filling method.

実斜䟋  脱脂粉乳1.36Kgポンドを撹拌䞋、37.8℃
100〓に加枩した党乳乳固圢分3.366
に加えた。埗られた混合物は乳固圢分含量玄13.7
および乳脂肪含量2.2であ぀た。混合物を
87.8℃190〓以䞊の枩床に加熱しお殺菌し、
37.8〜43.3℃100〜110〓に冷华し、混合物に
察しお重量1.36Kg、ポンドのラクトバ
チルス・ブルガリカスおよびスタフむロコツカ
ス・サヌモフむラス培逊菌を混合した。培逊を玄
5.5時間行ない、この間に圓初玄のPHは玄4.15
に䜎䞋した。぀いで、混合物の枩床を20〜25分を
芁しお60〜62.8℃140〜145〓に䞊げ、蛋癜を
前調敎した。぀いで、぀ぎの成分からなる也燥混
合物をその䞊に散垃した。
Example 2 1.36Kg (3 pounds) of skim milk powder was stirred at 37.8℃
Whole milk (milk solids 3.3%) heated to (100〓)66
added to. The resulting mixture has a milk solids content of approximately 13.7
% and milk fat content was 2.2%. mixture
Sterilize by heating to a temperature of 87.8℃ (190〓) or higher,
It was cooled to 37.8-43.3°C (100-110°C) and 2% by weight (1.36 Kg, 3 pounds) of Lactobacillus bulgaricus and Staphylococcus thermophilus cultures were mixed with the mixture. Culture approx.
It lasted for 5.5 hours, during which time the pH of about 6 at the beginning was about 4.15.
It declined to . The temperature of the mixture was then raised to 60-62.8°C (140-145°C) over 20-25 minutes to precondition the protein. A dry mixture consisting of the following ingredients was then sprinkled thereon.

ク゚ン酞 68.10.1重量 リゎヌムCDS 190.50.28重量 糖粉末ブドり糖 2.383.5重量 ペクチンJM 204.30.3重量 レゞスタ柱粉 816.61.2重量 埗られた混合物を703000Kgm21000psiよ
りわずかに䜎い圧力で15〜20分間段階で均質化
した。これにより所望のプレヌン・ペヌグルト68
Kg150ポンドが埗られ、぀いで、熱亀換噚䞭、
87.8℃190〓で分間加熱し、殺菌および柱
粉の糊化を完了し、所望の組織を埗た。実斜䟋
ず同様に補品を冷华し、無菌的に充填した。
Citric acid 68.1g (0.1% by weight) Ligome CDS 190.5g (0.28% by weight) Sugar (powdered glucose) 2.38g (3.5% by weight) Pectin JM 204.3g (0.3% by weight) Register starch 816.6g (1.2% by weight) Obtained The mixture was homogenized in one step for 15-20 minutes at a pressure slightly less than 1000 psi. This results in the desired plain yogurt68
Kg (150 lb) is obtained, then in the heat exchanger,
The mixture was heated at 87.8°C (190°C) for 2 minutes to complete sterilization and gelatinization of starch, thereby obtaining the desired tissue. Example 1
The product was cooled and filled aseptically.

明らかなように、所望により、該補品は実斜䟋
ず同様に果実−フレヌバヌ補品に倉えるこずが
できる。
As is clear, if desired, the product can be converted into a fruit-flavored product similar to Example 1.

実斜䟋  党乳乳固圢分3.553.5Kg96ポンドの
バツチを37.8℃100〓に加熱し、攪拌䞋、
の脱脂粉乳970、ポンドを加え、混合
物を87.8℃190〓で10分間加熱した。殺菌埌、
混合物を43.3℃110〓に冷华し、実斜䟋で
甚いたペヌグルト甚培逊菌970ポンドを
混合した。PHが4.25に䜎䞋するたで43.3℃110
〓で培逊を぀づけた〜4.5時間。
Example 3 A batch of 53.5 Kg (96 lb) of whole milk (milk solids 3.5%) was heated to 37.8°C (100 ml) and, under stirring,
% skimmed milk powder (970 g, 2 lbs.) was added and the mixture was heated to 87.8° C. (190° C.) for 10 minutes. After sterilization,
The mixture was cooled to 43.3°C (110°C) and 970g (2 pounds) of the yogurt culture used in Example 1 was mixed. 43.3℃ (110
〓) The culture was continued (4 to 4.5 hours).

別途、぀ぎの成分の也燥混合物を調補した。 Separately, a dry mixture of the following components was prepared.

ク゚ン酞 45.40.1重量 リゎヌムCDS 1270.28重量 糖 20434.5重量 ペクチンJM 136.20.3重量 レゞスタ柱粉 544.81.2重量 混合物54.4℃130〓に加枩し、培逊した基
質䞊に散垃し、぀いで、20分皋床を芁しお枩床を
62.8℃145〓に䞊昇させた。この間に所望の
蛋癜の前調敎が生じた。党混合物を703000Kgm2
1000psiの圧力䞋、玄20分間段階で均質化
し、぀いで、87.8℃190〓で分間殺菌した。
぀いで、容噚に充填前、補品を無菌条件䞋に保ち
ながら26.7℃80〓以䞋に冷华した。
Citric acid 45.4g (0.1% by weight) Rigoum CDS 127g (0.28% by weight) Sugar 2043g (4.5% by weight) Pectin JM 136.2g (0.3% by weight) Register starch 544.8g (1.2% by weight) Mixture at 54.4℃ (130〓) Spray on the heated and cultured substrate, then allow the temperature to rise over about 20 minutes.
The temperature was raised to 62.8℃ (145〓). During this time, preconditioning of the desired protein occurred. Total mixture 703000Kg/ m2
Homogenization was performed in one step under pressure (1000 psi) for approximately 20 minutes, followed by sterilization at 87.8°C (190°) for 2 minutes.
The product was then cooled to below 26.7°C (80°C) while maintaining sterile conditions before filling into containers.

前蚘のごずく、埗られた補品はプレヌン・ペヌ
グルトであり、実斜䟋ず同様にしお所望の果実
−フレヌバヌ補品に容易に倉えるこずができる。
As mentioned above, the resulting product is a plain yogurt and can be easily converted into the desired fruit-flavored product as in Example 1.

Claims (1)

【特蚱請求の範囲】  (a) 液䜓乳基質を、殺菌するに充分な時間高
枩に保持し、 (b) 殺菌した基質を玄37.8〜46.1℃玄100〜115
〓の培逊枩床たで冷华し、 (c) 該基質に乳酞を生成するペヌグルト甚培逊菌
を接皮し、該枩床でPHが玄4.5〜4.0に䜎䞋する
たで基質を培逊しおペヌグルト・ベヌスを埗、 (d) 該ペヌグルト・ベヌスが未だ高い枩床にある
間に぀ぎの成分 カラギヌナン 箄0.1〜0.8 ク゚ン酞むオン 箄0.05〜0.2 柱 粉 箄0.5〜1.5 砂 糖 箄2.0〜6.0 および、芁すれば 氎混合物党䜓の乳固圢分が玄10〜15ずなるよ
うな量 を添加、混合しはいずれも混合物党䜓に察
しおの重量、 (e) 埗られた倩然ペヌグルトを、柱粉の実質的な
糊化なしに蛋癜の前調敎が行なえる高枩時間
凊理に付し、 (f) 該混合物を最高玄76.7℃玄170〓の枩床
で、玄351500〜1054500Kgm2玄500〜
1500psiの圧力䞋、段階で均質化し、 (g) 所望により、均質化した混合物にフレヌバヌ
およびたたは銙料を加え、 (h) 埗られた混合物を少なくずも76.7℃170〓
の枩床で殺菌し、 (i) 殺菌したペヌグルトを29.4℃85〓以䞋に
冷华する、 こずを特城ずする殺菌ペヌグルトの補法。  該倩然ペヌグルトの枩床を培逊枩床以䞋に䜎
䞋させるこずなく、玄0.5〜分間で均質化枩床
たで䞊昇させ、工皋(d)の成分の添加を倩然ペヌグ
ルトの枩床が玄62.8℃玄145〓に達するたで
に完了する前蚘第項の補法。  該倩然ペヌグルトの枩床を玄60〜71.1℃玄
140〜160〓たで䞊昇させ、この枩床で〜20分
間保持しお該蛋癜の前調敎を行なう前蚘第項の
補法。  工皋(d)においお、該成分をペヌグルト・ベヌ
スの枩床が玄37.8〜46.1℃玄100〜115〓の培
逊枩床から玄29.4℃玄85〓たでに䜎䞋する間
に添加、混合し、所望により、その枩床を工皋(e)
の時間枩床凊理に付す前にさらに䜎䞋させる前
蚘第項の補法。  工皋(d)においお、さらに、倩然ペヌグルトに
基づいお0.5重量たでのペクチンをペヌグル
ト・ベヌスに添加する前蚘第項〜第項いずれ
か぀の補法。  工皋(f)の均質化を玄562400〜843600Kgm2
玄800〜1200psiで行なう前蚘第項〜第項
いずれか぀の補法。  工皋(d)においお、玄0.2〜0.5のカラギヌナ
ンを添加する前蚘第項〜第項いずれか぀の
補法。  工皋(d)においお、玄0.075〜0.05のク゚ン
酞むオンを添加する前蚘第項〜第項いずれか
぀の補法。  工皋(d)においお、玄0.75〜1.25の柱粉を加
える前蚘第項〜第項いずれか぀の補法。  工皋(d)においお、玄〜の砂糖を加え
る前蚘第項〜第項いずれか぀の補法。  工皋(b)の培逊枩床が玄42.2〜44.4℃玄
108〜112〓である前蚘第項〜第項いずれか
぀の補法。  工皋(a)の殺菌を、乳基質を玄87.8〜98.9℃
玄190〜210〓の枩床で玄30分たで加熱しお行
なう前蚘第項〜第項いずれか぀の補法。  工皋(d)においお、該成分を氎性スラリヌず
しお添加する前蚘第項〜第項いずれか぀の
補法。  乳基質の総乳固圢分含量が17〜19重量で
ある前蚘第項〜第項いずれか぀の補法。
[Scope of Claims] 1. (a) maintaining a liquid milk substrate at a high temperature for a period sufficient to sterilize the substrate;
(c) Inoculate the substrate with yogurt culture bacteria that produce lactic acid, and culture the substrate at the temperature until the pH drops to about 4.5 to 4.0 to obtain a yogurt base. (d) While the yogurt base is still at elevated temperature, the following ingredients are added: carrageenan about 0.1-0.8% citrate ions about 0.05-0.2% starch about 0.5-1.5% sugar about 2.0-6.0% and as necessary. Then, add and mix an amount such that the milk solids content of the entire water mixture is about 10-15% (all percentages are % by weight based on the total mixture), (e) the resulting natural yogurt, (f) subjecting the mixture to a high temperature/time treatment that preconditions the protein without substantial gelatinization of the starch ; (about 500~
(g) optionally add flavors and/or fragrances to the homogenized mixture; (h) heat the resulting mixture to at least 76.7°C (170°C);
A method for producing sterilized yogurt, characterized by: (i) cooling the sterilized yogurt to 29.4℃ (85〓) or below. 2. Raise the temperature of the natural yogurt to the homogenization temperature in about 0.5 to 5 minutes without lowering it below the culture temperature, and add the ingredients in step (d) until the temperature of the natural yogurt is about 62.8 °C (about 145 °C). ). 3. Set the temperature of the natural yogurt to about 60 to 71.1°C (approx.
140-160〓) and held at this temperature for 5-20 minutes to pre-condition the protein. 4. In step (d), the ingredients are added and mixed while the temperature of the yogurt base is reduced from the incubation temperature of about 37.8-46.1°C (about 100-115°) to about 29.4°C (about 85°). , if desired, adjust the temperature in step (e)
The process of item 1 above, wherein the temperature is further reduced before subjecting to the time/temperature treatment. 5. The method of any one of paragraphs 1 to 4 above, wherein in step (d), furthermore, up to 0.5% by weight of pectin, based on the natural yogurt, is added to the yogurt base. 6 Homogenization in step (f) approximately 562400 to 843600Kg/m 2
(about 800 to 1200 psi). 7. The method according to any one of Items 1 to 4 above, wherein in step (d), about 0.2 to 0.5% carrageenan is added. 8. The method according to any one of Items 1 to 4 above, wherein in step (d), about 0.075 to 0.05% of citrate ions are added. 9. The method according to any one of Items 1 to 4 above, wherein in step (d), about 0.75 to 1.25% starch is added. 10. The method according to any one of Items 1 to 4 above, wherein in step (d), about 4 to 5% sugar is added. 11 The culture temperature in step (b) is approximately 42.2 to 44.4℃ (approximately
108 to 112〓). 12 Sterilize the milk substrate in step (a) at approximately 87.8-98.9℃.
(about 190 to 210〓) for up to about 30 minutes. 13. The method according to any one of Items 1 to 4 above, wherein in step (d), the component is added as an aqueous slurry. 14. The method according to any one of Items 1 to 4 above, wherein the total milk solids content of the milk substrate is 17 to 19% by weight.
JP2197483A 1982-02-11 1983-02-12 Production of sterilized yoghurt Granted JPS58152444A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US34796182A 1982-02-11 1982-02-11
US347961 1982-02-11

Publications (2)

Publication Number Publication Date
JPS58152444A JPS58152444A (en) 1983-09-10
JPH049503B2 true JPH049503B2 (en) 1992-02-20

Family

ID=23366050

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Application Number Title Priority Date Filing Date
JP2197483A Granted JPS58152444A (en) 1982-02-11 1983-02-12 Production of sterilized yoghurt

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Country Link
JP (1) JPS58152444A (en)
CA (1) CA1182682A (en)

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AR231215A1 (en) * 1982-06-15 1984-10-31 Cpc International Inc PROCEDURE FOR THE PREPARATION OF AN ACIDIFIED DAIRY PRODUCT AND PRODUCT SO OBTAINED
US4748026A (en) * 1986-08-15 1988-05-31 Nabisco Brands, Inc. Process for production of a no-starch shelf stable yogurt product
JP3888798B2 (en) * 1999-05-11 2007-03-07 カルピス株匏䌚瀟 Method for producing fermented milk beverage with enhanced fermentation flavor and stability
JP5354560B2 (en) * 2007-04-06 2013-11-27 地方独立行政法人北海道立総合研究機構 Fermented milk paste and method for producing the same
SE533537C2 (en) * 2009-06-18 2010-10-19 Tetra Laval Holdings & Finance Method for making a yogurt-based product
IN2015DN01696A (en) * 2012-09-12 2015-07-03 Nestec Sa
JP2017534291A (en) * 2014-11-14 2017-11-24 アヌラ フヌズ ゚゚ムビ゚   Whey protein-based high protein yogurt-like product, ingredients suitable for its production, and method of production

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CA1182682A (en) 1985-02-19

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