JPS62240A - Production of calcium coagulated cheese from ultrafiltered and concentrated milk - Google Patents

Production of calcium coagulated cheese from ultrafiltered and concentrated milk

Info

Publication number
JPS62240A
JPS62240A JP5169786A JP5169786A JPS62240A JP S62240 A JPS62240 A JP S62240A JP 5169786 A JP5169786 A JP 5169786A JP 5169786 A JP5169786 A JP 5169786A JP S62240 A JPS62240 A JP S62240A
Authority
JP
Japan
Prior art keywords
milk
concentrated
rennet
concentrated milk
casein
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.)
Pending
Application number
JP5169786A
Other languages
Japanese (ja)
Inventor
Masanobu Kamitake
神武 正信
Yukio Uchida
幸生 内田
Takayoshi Sato
孝義 佐藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SHOKUHIN SANGYO MAKU RIYOU GIJUTSU KENKYU KUMIAI
Original Assignee
SHOKUHIN SANGYO MAKU RIYOU GIJUTSU KENKYU KUMIAI
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 by SHOKUHIN SANGYO MAKU RIYOU GIJUTSU KENKYU KUMIAI filed Critical SHOKUHIN SANGYO MAKU RIYOU GIJUTSU KENKYU KUMIAI
Publication of JPS62240A publication Critical patent/JPS62240A/en
Pending legal-status Critical Current

Links

Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23CDAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
    • A23C19/00Cheese; Cheese preparations; Making thereof
    • A23C19/02Making cheese curd
    • A23C19/028Making cheese curd without substantial whey separation from coagulated milk
    • A23C19/0285Making cheese curd without substantial whey separation from coagulated milk by dialysis or ultrafiltration

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  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Dairy Products (AREA)

Abstract

PURPOSE:To produce cheese continuously in a short time, by subjecting a concentrated milk concentrated by ultrafiltration to rennet reaction and adding a water-soluble calcium salt thereto to coagulate the concentrated milk. CONSTITUTION:Raw material milk consisting of cow's milk or modified milk or raw material milk prepared by adding lactic acid bacteria or lactic acid to cow's milk or modified milk and acidified is concentrated by ultrafiltration and dialysis and filtration in combination to give concentrated milk. About 15-35ppm/kg concentrated milk rennet and, as necessary, lactic acid bacterial starter are added to the above-mentioned concentrated milk to carry out the rennet reaction of the kappa-casein in the concentrated milk into para-kappa-casein. When the above-mentioned rennet reaction proceeds, a water-soluble calcium salt, e.g. calcium chloride, is added to coagulate the concentrated milk and whey is removed by pressing and heating and aging the resultant curd.

Description

【発明の詳細な説明】 良栗上■貫朋公団 本発明は、限外濾過により濃縮された濃縮原料乳の凝固
(カード化)を水溶性カルシウム塩の添加により極めて
短時間で行うことにより、チーズを連続方式で製造する
方法に関する。
[Detailed Description of the Invention] Ryoguri Kami ■Kanho Public Corporation The present invention coagulates (curds) concentrated raw milk concentrated by ultrafiltration in an extremely short time by adding water-soluble calcium salt. It relates to a method for producing cheese in a continuous manner.

従来の技術 従来、チーズの製造は一般に、原料乳に乳酸菌スタータ
ーを添加して醗酵させ、次いでレンネットを添加して凝
固(カード化)させることにより行われている。また、
チーズの収率を高めるために限外濾過により濃縮された
濃縮乳を原料乳として用いることも行われている。しか
し、このような従来法では原料乳並びに濃縮乳のレンネ
ットによる凝固にはレンネットの力価等により異なるも
のの、通常30〜60分間の静置時間を要するものであ
り、したがって、チーズを連続方式で製造することは実
際上不可能であった。
BACKGROUND OF THE INVENTION Conventionally, cheese production has generally been carried out by adding lactic acid bacteria starter to raw milk for fermentation, and then adding rennet to coagulate (curd) the milk. Also,
In order to increase the yield of cheese, concentrated milk concentrated by ultrafiltration is also used as raw material milk. However, in such conventional methods, coagulation of raw milk and concentrated milk with rennet usually requires a standing time of 30 to 60 minutes, although this varies depending on the rennet strength, etc. Therefore, it is necessary to continuously freeze cheese. It was practically impossible to manufacture using this method.

日が”′ しようとする課 従来のチーズ製造法における牛乳の凝固機構は、レンニ
ンによる牛乳中のκ−カゼインのパラ−κ−カゼイン化
及びその後のバラーχ−カゼインとカルシウムイオンの
結合によるものとされている。
The coagulation mechanism of milk in the conventional cheese manufacturing method is based on the conversion of κ-casein in milk to para-κ-casein by rennin and the subsequent binding of bulk χ-casein to calcium ions. has been done.

而して、本発明者は、限外濾過及び透析濾過に付した濃
縮乳の成分を検討した結果、該濃縮乳にはレンネット凝
固に関与するカルシウムイオンが極端に低減しているこ
とを見出した。すなわち、上記濃縮乳においてはレンニ
ンによるκ−カゼインのパラ−κ−カゼイン化後のパラ
−κ−カゼインとカルシウムイオンの結合が阻害される
ため、該濃縮乳に水溶性カルシウム塩を添加することに
よる静置での凝固が極めて短時間で行い得ることの知見
を得て本発明をなすに至った。
As a result of examining the components of concentrated milk subjected to ultrafiltration and diafiltration, the present inventor found that calcium ions involved in rennet coagulation were extremely reduced in the concentrated milk. Ta. That is, in the above concentrated milk, the binding of para-κ-casein and calcium ions after the conversion of κ-casein to para-κ-casein by rennin is inhibited. The present invention was made based on the knowledge that solidification by standing still can be carried out in an extremely short time.

したがって、本発明は、限外濾過濃縮乳からのチーズ製
造における静置凝固時間を短縮することにより、チーズ
の製造工程を簡易化して連続方式で製造し得るチーズの
製造方法を提供することを目的とする。以下本発明の詳
細な説明する。
Therefore, an object of the present invention is to provide a method for manufacturing cheese that can be manufactured in a continuous manner by simplifying the cheese manufacturing process by shortening the standing solidification time in cheese manufacturing from ultrafiltered concentrated milk. shall be. The present invention will be explained in detail below.

又皿(2)且底 本発明の特徴は、牛乳又は加工乳を、限外濾過と透析濾
過(Dia(1)tration)を組合わせた処理に
付して濃縮し、得られた濃縮乳に乳酸菌スターター及び
レンネットを添加して該濃縮乳中のκ−カゼインをパラ
−κ−カゼイン化するレンネット反応を行った後、水溶
性カルシウム塩を添加して凝固させることによりチーズ
を製造することにある。
Dish (2) and bottom A feature of the present invention is that milk or processed milk is subjected to a treatment that combines ultrafiltration and diafiltration (Dia(1) tration) to concentrate it, and lactic acid bacteria are added to the resulting concentrated milk. After adding a starter and rennet to perform a rennet reaction to convert κ-casein in the concentrated milk into para-κ-casein, cheese is produced by adding a water-soluble calcium salt and coagulating it. be.

また、本発明は、牛乳又は加工乳に乳酸菌スターター又
は乳酸を添加して酸性化したものを原料乳としてmい、
この原料乳を一眼外濾過と透析濾過を組合わせた処理に
付して濃縮し、得られた濃縮乳にレンネットを添加して
該濃縮乳中のκ−カゼインをパラ−κ−カゼイン化する
レンネット反応を行った後、水溶性カルシウム塩を添加
して凝固させることによりチーズを製造することも特徴
とする。なお、ここでいう“加工乳”とは粉乳を水に熔
解して得られる還元牛乳、全乳と脱脂乳を配合した調合
牛乳を意味する。
In addition, the present invention uses milk or processed milk that has been acidified by adding lactic acid bacteria starter or lactic acid as raw milk,
This raw milk is concentrated by a combination of single-lens filtration and diafiltration, and rennet is added to the obtained concentrated milk to convert κ-casein in the concentrated milk to para-κ-casein. Another feature is that cheese is produced by performing a rennet reaction and then adding a water-soluble calcium salt and coagulating it. Note that "processed milk" as used herein means reduced milk obtained by dissolving powdered milk in water, and mixed milk that is a mixture of whole milk and skim milk.

i を解ンするための 本発明は、まず、牛乳又は加工乳からなる原料乳、もし
くは牛乳又は加工乳に乳酸菌スターター又は乳酸を添加
して酸性化した原料乳を、限外濾過と透析濾過を組合わ
せて処理することにより濃縮して濃縮乳を調製する。こ
の場合における上記の組合わせ処理は、原料乳を限外濾
過により処理して約2〜10の濃縮倍率に濃縮したもの
を透析濾過により処理してもよく、更に透析濾過による
処理を行った後再び限外濾過により濃縮してもよい。
In order to solve the problem, the present invention first involves ultrafiltration and diafiltration of raw milk consisting of cow's milk or processed milk, or raw milk that has been acidified by adding lactic acid bacteria starter or lactic acid to cow's milk or processed milk. The combined processing is concentrated to prepare concentrated milk. In this case, the above combination treatment may be performed by treating raw milk by ultrafiltration, concentrating it to a concentration ratio of about 2 to 10, and then treating it by diafiltration, and then further treating it by diafiltration. It may be concentrated again by ultrafiltration.

また、原料乳を透析濾過処理し、次いで限外濾過処理し
てもよい。なお、上記濃縮乳の調製に際し、限外濾過に
よる原料乳の濃縮倍率を高くするに伴い、透析濾過の処
理に要する時間が長くなるけれども、得られる透過液の
濃度が高くなり、一方、限外a過による上記濃縮倍率を
低くすると透析濾過の処理に要する時間が短くなるけれ
ども、得られる透過液の濃度は低くなる。
Alternatively, raw milk may be subjected to diafiltration treatment and then ultrafiltration treatment. In addition, when preparing the above-mentioned concentrated milk, as the concentration ratio of the raw milk by ultrafiltration is increased, the time required for the diafiltration process becomes longer, but the concentration of the obtained permeate increases. If the concentration ratio by a-filtration is lowered, the time required for the diafiltration process will be shortened, but the concentration of the obtained permeate will be lower.

したがって、上記原料乳からの濃縮乳の調製に当っては
、原料乳の可溶性カルシウム含量並びに得られる濃縮乳
の所望な濃度を考慮して限外濾過による原料乳の濃縮倍
率を調整するとよい。
Therefore, when preparing concentrated milk from the raw milk, the concentration ratio of the raw milk by ultrafiltration may be adjusted in consideration of the soluble calcium content of the raw milk and the desired concentration of the obtained concentrated milk.

しかし、限外濾過による原料乳の濃縮倍率を高くすると
共に透析濾過による原料乳中の可溶性カルシウム金星の
低下を大きくすることが好ましい。
However, it is preferable to increase the concentration ratio of raw milk by ultrafiltration and to increase the decrease in soluble calcium Venus in raw milk by diafiltration.

本発明によると、可溶性カルシウム含量を最初の原料乳
中の各濃度の1/10〜l/30程度までに低減するこ
とができる。原料乳を限外濾過により濃縮して得られる
濃縮乳は、透析濾過を行うことに関係なくリーテンテー
トと称せられる。
According to the present invention, the soluble calcium content can be reduced to about 1/10 to 1/30 of each concentration in the initial raw milk. Concentrated milk obtained by concentrating raw milk by ultrafiltration is called retentate regardless of whether diafiltration is performed.

本発明では、次いで上記濃縮乳に、原料乳として牛乳又
は加工乳を用いた場合には、乳酸菌スターター及びレン
ネットを添加し、一方原料乳として酸性化した牛乳又は
加工乳を用いた場合には、レンネットを添加して濃縮乳
中のκ−カゼインのパラ−κ−カゼイン化へのレンネッ
ト反応を行わせる。このレンネット反応においては、濃
縮乳中の可溶性カルシウム含量が原料乳に比し著しく低
いので、通常の牛乳や加工乳にレンネットを添加してレ
ンネット反応を行わせるチーズの製造の場合における凝
固時間(30〜60分)では乳の凝固は起らない。ここ
で用いるレンネットは子牛レンネットもしくは微生物レ
ンネットであってもよく、通常15〜35ppm/kg
濃縮乳添加する。
In the present invention, lactic acid bacteria starter and rennet are then added to the concentrated milk when cow's milk or processed milk is used as the raw material milk, whereas when acidified milk or processed milk is used as the raw material milk, the lactic acid bacteria starter and rennet are added to the concentrated milk. , rennet is added to carry out the rennet reaction to convert κ-casein in concentrated milk to para-κ-casein. In this rennet reaction, since the soluble calcium content in concentrated milk is significantly lower than that in raw milk, rennet is added to regular milk or processed milk to cause the rennet reaction. Coagulation of the milk does not occur during the time (30-60 minutes). The rennet used here may be calf rennet or microbial rennet, and usually has a concentration of 15 to 35 ppm/kg.
Add concentrated milk.

本発明は上記濃縮乳のレンネット反応が進行した時点で
水溶性カルシウム塩、例えば塩化カルシウムを添加する
ことにより濃縮乳に凝固を起させる。水溶性カルシウム
塩の添加による濃縮乳の凝固は、Mi1m乳中の可溶性
カルシウムの濃度及び水溶性カルシウム塩の添加量によ
り異なるも、1分乃至数分程度の極めて短時間で行われ
る。すなわち、濃縮乳中の可溶性カルシうムの温度及び
レンネット反応後に添加する水溶性カルシウム塩の世を
調節することにより、濃縮乳の凝固時間及び凝固により
得られるカードの凝塊物性をコントロールすることが可
能となる。また、濃縮乳に添加した乳酸菌スターターの
活性を損わない程度の高い濃度、例えば37〜38℃の
温度に保持することにより、もしくはレンネットの添加
量を多くすることによっても上記凝固に要する水溶性カ
ルシウム塩の添加量を低減することができる。
In the present invention, when the rennet reaction of the concentrated milk has progressed, a water-soluble calcium salt, such as calcium chloride, is added to cause the concentrated milk to coagulate. Coagulation of concentrated milk by the addition of water-soluble calcium salt is carried out in a very short time of about 1 to several minutes, although it varies depending on the concentration of soluble calcium in Mi1m milk and the amount of water-soluble calcium salt added. That is, by adjusting the temperature of soluble calcium in concentrated milk and the level of water-soluble calcium salt added after the rennet reaction, the coagulation time of concentrated milk and the physical properties of the coagulated curd obtained by coagulation can be controlled. becomes possible. In addition, by maintaining the lactic acid bacteria starter added to the concentrated milk at a high concentration that does not impair the activity, for example, at a temperature of 37 to 38°C, or by increasing the amount of rennet added, it is possible to dissolve the water required for coagulation. The amount of calcium salt added can be reduced.

上述のようにして濃縮乳を凝固させて得られたカードを
賽の目状に細切し、加温した後型詰めしプレスによりホ
エーを排除し、加温して熟成させてチーズ製品を得る。
The curd obtained by coagulating the concentrated milk as described above is cut into dice, warmed, packed in a mold, whey is removed by a press, heated and aged to obtain a cheese product.

叙上のように、本発明に従って原料乳から調製した濃縮
乳にレンネット反応を行わせた後に、水溶性カルシウム
塩を添加すると極めて短時間で乳の凝固を起させること
ができるので、チーズの製造上置も重要な工程であるカ
ードの造成工程をレンネット反応のみに基づ〈従来法の
ように静置法で行うことなく、簡易かつ効率的に実施し
得るようになる。
As mentioned above, adding a water-soluble calcium salt to concentrated milk prepared from raw milk according to the present invention after performing a rennet reaction can cause milk to coagulate in a very short time. The card making process, which is also an important step in production, can be carried out simply and efficiently based only on the rennet reaction (without using the static method as in the conventional method).

したがって、本発明によると、上述のようにしてレンネ
ット反応を行わせた濃縮乳の移送段階で水溶性カルシウ
ム塩を添加することによりカード化を行い得るので、チ
ーズの製造工程を連続方式にすることも可能となる。
Therefore, according to the present invention, curd formation can be carried out by adding a water-soluble calcium salt during the transfer stage of the concentrated milk subjected to the rennet reaction as described above, thereby making the cheese manufacturing process a continuous process. It also becomes possible.

以下に実施例を示して本発明をさらに具体的に説明する
EXAMPLES The present invention will be explained in more detail with reference to Examples below.

実施例 1 全固形分11.9%、脂肪3.3%及び蛋白質3.1%
、乳糖4.6%可溶性カルシウム36.5■/100 
gを含有する牛乳120 kgを、65℃で30分間低
温殺菌し、50℃に冷却したものを、ローヌプーランt
lFP10モジュール膜面積: 0.88rrr (I
RIS 303B膜)を用いたIIF回分濃縮プラント
で限外濾過に付し、濃縮倍率2.5に濃縮した濃縮乳4
8kgを調製し、この濃縮乳48kgについて定容量透
析濾過゛(透過流束に見合った水の補給)を補給水量が
48kgになるまで行なった。ついで得られた乳を再度
上記の限外濾過に付して濃縮倍率5に濃縮して濃縮乳2
4kgを得た。
Example 1 Total solids 11.9%, fat 3.3% and protein 3.1%
, lactose 4.6% soluble calcium 36.5■/100
Rhône-Poulenc T
lFP10 module membrane area: 0.88rrr (I
Concentrated milk 4 was subjected to ultrafiltration in an IIF batch concentration plant using RIS 303B membrane) and concentrated to a concentration ratio of 2.5.
8 kg of concentrated milk was prepared, and 48 kg of this concentrated milk was subjected to constant volume diafiltration (replenishment of water commensurate with the permeation flux) until the amount of replenishment water reached 48 kg. Then, the obtained milk is again subjected to the above-mentioned ultrafiltration and concentrated to a concentration ratio of 5 to obtain concentrated milk 2.
I got 4 kg.

このようにして得られた濃縮乳中の可溶性カルシウムの
濃度は17.5■/100gであって、最初に用いた牛
乳に比して1/11に低減した。
The concentration of soluble calcium in the concentrated milk thus obtained was 17.5 μ/100 g, which was reduced to 1/11 compared to the milk originally used.

次に、上記濃縮乳の20kgを秤量し、30℃に冷却し
た後、これに乳酸菌スターターとして凍結濃縮RD−ス
ターターカルチャー0.2重量%を接種してpHを6.
2以下とし、ついでレンネット(クリスチャン・ハンセ
ン社製) 30ppmを加えて20分間レン7ット反応
を行ない、ついで、濃縮乳量に対して塩化カルシウム0
:10%を水溶液として攪拌下に添加した。添加後約1
分間で乳が凝固した。
Next, 20 kg of the above concentrated milk was weighed and cooled to 30°C, and then 0.2% by weight of frozen concentrated RD-starter culture was inoculated thereto as a lactic acid bacteria starter to adjust the pH to 6.
2 or less, then add 30 ppm of rennet (manufactured by Christian Hansen) and carry out a rennet reaction for 20 minutes.
:10% was added as an aqueous solution under stirring. Approximately 1 after addition
The milk curdled within minutes.

得られたカード(凝塊)を1CI11の賽の目状に細切
し、30〜38℃に加温した後、型詰めしてプレスを行
なってホエーを排除した。得られたプレスカードを20
%の食塩水溶液に約10時間浸漬して加塩を施し、いわ
ゆるヤングチーズ約9 kgを得た。ヤングチーズを3
ケ月間熟成して製品とする。
The obtained curd (coagulum) was cut into 1 CI 11 dice, heated to 30 to 38°C, packed into a mold, and pressed to remove whey. 20 of the obtained press cards
% salt aqueous solution for about 10 hours to add salt to obtain about 9 kg of so-called young cheese. 3 pieces of young cheese
The product is aged for several months.

上記ヤングチーズは全固形分55.0%、脂肪28.3
%及び蛋白質24.4%を含有する。
The above young cheese has a total solid content of 55.0% and a fat of 28.3%.
% and contains 24.4% protein.

実施例2 全固形分9.16%、蛋白質3,2、乳ill!4.4
%、可溶性カルシウム37.6■/100 gを含有す
る脱脂乳120 kgを、65℃で30分間低温殺菌し
、10℃に冷却したものに、乳酸(特級)55  mj
!添加しpHを6.48にし、−夜装置した。これを5
0℃に加温し、ローヌプーランIIFP 10モジユ一
ル膜面積: 0.88(IRIS 3o38  tlり
を用いたIIF回分濃縮プラントで限外濾過に付し、濃
縮倍率2.5に濃縮した濃縮乳48kgを調製し、この
濃縮乳48kgに、定容g透析濾過(透過流束に見合っ
た水の補給)を補給水量が48kgになるまで行なった
。ついで得られた乳を再度上記の限外濾過に付して濃縮
倍率5に濃縮して濃縮乳24kgを得た。このようにし
て得られた濃縮乳中の可溶性カルシウムの濃度は21.
9■/100gであって、最初に用いた脱脂乳に比して
、l/9量に低減した。
Example 2 Total solids 9.16%, protein 3.2, milk ill! 4.4
%, soluble calcium/100 g was pasteurized at 65°C for 30 minutes and cooled to 10°C, and added with 55 mj of lactic acid (special grade).
! The pH was adjusted to 6.48 and the unit was heated overnight. This is 5
Concentrated milk was heated to 0°C and subjected to ultrafiltration in an IIF batch concentration plant using a Rhone-Poulenc IIFP 10 module membrane area: 0.88 (IRIS 3o38 tl) to a concentration ratio of 2.5. 48 kg of concentrated milk was prepared, and this 48 kg of concentrated milk was subjected to constant volume g diafiltration (replenishment of water commensurate with the permeation flux) until the amount of replenishment water reached 48 kg.Then, the obtained milk was again subjected to the above ultrafiltration. The concentrated milk was concentrated to a concentration factor of 5 to obtain 24 kg of concentrated milk.The concentration of soluble calcium in the concentrated milk thus obtained was 21.
The amount was reduced to 1/9 of the amount of skim milk used initially.

次に、上記濃縮乳の20kgを秤量し、35℃に冷却し
た後、レンネット(クリスチャン・ハンセン社製)15
ppmを加えて、20分間レンネット反応を行ない、t
rami乳量に対し塩化カルシウム0.1%を水溶液と
して撹拌下に添加した。添加後約1分間で乳が凝固した
Next, 20 kg of the above concentrated milk was weighed, cooled to 35°C, and then 15 kg of rennet (manufactured by Christian Hansen) was weighed and cooled to 35°C.
ppm and carry out the rennet reaction for 20 minutes.
rami milk, 0.1% calcium chloride was added as an aqueous solution under stirring. The milk coagulated about 1 minute after addition.

得られたカード(凝塊)をl cmの賽の目状に細切し
、30〜38℃に加温した後、型詰めしてプレスを行な
ってホエーを排除した。得られたプレスカードをプロセ
スチーズの調合原料として配合率0%、10%、20%
、30%、40%、50%に変えて行った。風味として
は、30%を越えると差が感じられるものの、全体的に
は、大きな欠陥はないと判断でき、また組織も大差はな
い結果となった。
The obtained curd (coagulum) was cut into 1 cm dice, heated to 30 to 38° C., then packed into a mold and pressed to remove whey. The obtained press curd is used as a blending raw material for processed cheese at a blending rate of 0%, 10%, and 20%.
, 30%, 40%, and 50%. Although a difference in flavor can be felt when it exceeds 30%, it can be judged that there are no major defects overall, and there is no significant difference in texture.

Claims (2)

【特許請求の範囲】[Claims] (1)牛乳又は加工乳を、限外濾過と透析濾過を組合わ
せた処理に付して濃縮し、得られた濃縮乳に乳酸菌スタ
ーター及びレンネットを添加して該濃縮乳中のκ−カゼ
インをパラ−κ−カゼイン化するレンネット反応を行つ
た後、水溶性カルシウム塩を添加して凝固させることを
特徴とするカルシウム凝固チーズの製造方法。
(1) Milk or processed milk is subjected to a treatment combining ultrafiltration and diafiltration to concentrate, and lactic acid bacteria starter and rennet are added to the obtained concentrated milk to obtain κ-casein in the concentrated milk. A method for producing calcium coagulated cheese, which comprises performing a rennet reaction to convert para-κ-casein into para-κ-casein, and then adding a water-soluble calcium salt to coagulate the cheese.
(2)牛乳又は加工乳に乳酸菌スターター又は乳酸を添
加して酸性化したものを、限外濾過と透析濾過を組合わ
せた処理に付して濃縮し、得られた濃縮乳にレンネット
を添加して該濃縮乳中のκ−カゼインのパラ−κ−カゼ
イン化するレンネット反応を行つた後、水溶性カルシウ
ム塩を添加して凝固させることを特徴とするカルシウム
凝固チーズの製造方法。
(2) Milk or processed milk is acidified by adding lactic acid bacteria starter or lactic acid, and then concentrated through a combination of ultrafiltration and diafiltration, and rennet is added to the resulting concentrated milk. A method for producing calcium coagulated cheese, which comprises carrying out a rennet reaction to convert κ-casein in the concentrated milk into para-κ-casein, and then adding a water-soluble calcium salt to coagulate the cheese.
JP5169786A 1985-03-26 1986-03-10 Production of calcium coagulated cheese from ultrafiltered and concentrated milk Pending JPS62240A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP60-61717 1985-03-26
JP6171785 1985-03-26

Publications (1)

Publication Number Publication Date
JPS62240A true JPS62240A (en) 1987-01-06

Family

ID=13179256

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5169786A Pending JPS62240A (en) 1985-03-26 1986-03-10 Production of calcium coagulated cheese from ultrafiltered and concentrated milk

Country Status (4)

Country Link
JP (1) JPS62240A (en)
AU (1) AU583362B2 (en)
FR (1) FR2579421B1 (en)
NZ (1) NZ215558A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995000032A1 (en) * 1993-06-28 1995-01-05 Unilever N.V. Reduced fat renneted cheese product and a process of manufacturing it
JP2006528487A (en) * 2003-07-24 2006-12-21 フォンテラ コ−オペレイティブ グループ リミティド Concentrated milk protein component and method for preparing processed cheese therefrom
JP2011502511A (en) * 2007-11-07 2011-01-27 レプリノ フーズ カンパニー Method for producing skim milk powder for cheese production

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2663637B1 (en) * 1990-06-25 1992-09-18 Eurial PROCESS AND DEVICE FOR OBTAINING BETA CASEIN.
DE4326665C2 (en) * 1993-08-09 1995-07-13 Biotest Pharma Gmbh Process for sterile filtration of milk

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1433205A (en) * 1965-05-14 1966-03-25 Inst Przemyslu Mleczarskiego Process for the continuous production of maturing rennet cheese
DE2853045C2 (en) * 1978-12-08 1986-11-13 Günter Horst 7927 Sontheim Röhm Drill chuck
BG29737A1 (en) * 1979-09-13 1981-02-16 Dimitrov Method for continuous turning into cheese of milk by the production of white brined cheese and other soft cheeses

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995000032A1 (en) * 1993-06-28 1995-01-05 Unilever N.V. Reduced fat renneted cheese product and a process of manufacturing it
JP2006528487A (en) * 2003-07-24 2006-12-21 フォンテラ コ−オペレイティブ グループ リミティド Concentrated milk protein component and method for preparing processed cheese therefrom
JP2011502511A (en) * 2007-11-07 2011-01-27 レプリノ フーズ カンパニー Method for producing skim milk powder for cheese production
JP2014027957A (en) * 2007-11-07 2014-02-13 Leprino Foods Co Powdery milk composition and method for manufacturing cheese product using the same

Also Published As

Publication number Publication date
AU583362B2 (en) 1989-04-27
NZ215558A (en) 1988-11-29
FR2579421B1 (en) 1991-01-11
FR2579421A1 (en) 1986-10-03
AU5498586A (en) 1986-10-02

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