JPH0884576A - Production of low-acidic beverage filled in hermetically sealed container - Google Patents

Production of low-acidic beverage filled in hermetically sealed container

Info

Publication number
JPH0884576A
JPH0884576A JP6250077A JP25007794A JPH0884576A JP H0884576 A JPH0884576 A JP H0884576A JP 6250077 A JP6250077 A JP 6250077A JP 25007794 A JP25007794 A JP 25007794A JP H0884576 A JPH0884576 A JP H0884576A
Authority
JP
Japan
Prior art keywords
container
heat treatment
milk
retort
heat
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
JP6250077A
Other languages
Japanese (ja)
Inventor
Keizo Tsuji
慶三 辻
Taketo Ifuku
威人 伊福
Tomotaka Ootsuki
智香 大槻
Tomoyuki Fujii
友幸 藤井
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.)
Toyo Seikan Group Holdings Ltd
Original Assignee
Toyo Seikan Kaisha Ltd
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 Toyo Seikan Kaisha Ltd filed Critical Toyo Seikan Kaisha Ltd
Priority to JP6250077A priority Critical patent/JPH0884576A/en
Publication of JPH0884576A publication Critical patent/JPH0884576A/en
Pending legal-status Critical Current

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  • Dairy Products (AREA)
  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
  • Non-Alcoholic Beverages (AREA)

Abstract

PURPOSE: To obtain the beverage capable of suppressing the growth of thermostable microorganisms by mixing and homogenizing a low-acidic beverage content liquid containing milk without containing a sucrose ester of a fatty acid, heat-treating the resultant homogenate under specific conditions, then filling the heat-treated beverage in a container, hermetically sealing the container and carrying out the retort heat treatment. CONSTITUTION: This method for producing a low-acidic beverage filled in a hermetically sealed container is to mix cow's milk with granulated sugar, a skimmilk powder, a powdery coffee, sodium bicarbonate and water treated with active carbon, prepare a low-acidic beverage content liquid containing the milk without containing a sucrose ester of a fatty acid, carry out the heat treatment with a heat exchanger before or after performing the homogenizing treatment with a homogenizer, etc., then fill the resultant liquid in a container at <=35 deg.C filling temperature with a filler, replace air in the container with steam or a mixed gas of the steam with nitrogen gas, hermetically seal the container and subsequently perform the retort heat treatment. The sum total of the F0 value for the heat treatment with the heat exchanger and the retort heat treatment (heating time required to kill all the microorganisms) is >=120. The resultant beverage is capable of suppressing the germination and growth of thermostable microorganisms even by heating and selling thereof with an automatic vender, etc.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、缶入りコーヒー牛乳、
缶入りココア、缶入りミルクコーヒー、缶入りカフェオ
ーレ等の密閉容器入り低酸性飲料に関し、特に自動販売
機による加温販売に適した密閉容器入り低酸性飲料に関
する。
BACKGROUND OF THE INVENTION The present invention relates to canned coffee milk,
The present invention relates to a low-acidic beverage contained in a hermetically-sealed container such as canned cocoa, canned milk coffee, or canned cafe ole, and more particularly to a low-acidic beverage contained in a hermetically sealed container suitable for hot sale by a vending machine.

【0002】[0002]

【従来の技術】近年自動販売機の発達に伴い、コーヒー
牛乳等のミルク入り低酸性飲料の自動販売機中による販
売も増大している。乳飲料等の低酸性飲料を自動販売機
で45〜65℃の加温販売する場合に生じる問題の一つ
に耐熱性細菌の発芽増殖による内容物のフラットサワー
状の変敗がある。
2. Description of the Related Art With the development of vending machines in recent years, sales of low-acidic beverages containing milk such as coffee milk in vending machines are also increasing. One of the problems that occurs when low-acidic beverages such as milk beverages are sold at a temperature of 45 to 65 ° C. in a vending machine is flat sour deterioration of the contents due to germination and growth of heat-resistant bacteria.

【0003】このような耐熱性細菌の発芽増殖を抑制す
るために蔗糖脂肪酸エステルを飲料に添加することが有
効であることが知られており、たとえば特公昭57−2
6104号公報にはコーヒー乳飲料に対する蔗糖脂肪酸
エステルの実用的添加量は0.01%〜0.2%程度で
あることが記載されている(公報第5欄第4行〜第8
行)。
It is known that it is effective to add a sucrose fatty acid ester to a beverage in order to suppress the germination and growth of such thermostable bacteria. For example, Japanese Patent Publication No. 57-2.
Japanese Patent No. 6104 describes that the practical addition amount of sucrose fatty acid ester to a coffee milk drink is about 0.01% to 0.2% (publication column 5, line 4, line 8).
line).

【0004】また、上記特公昭57−26104号公報
には記載のない乳飲料中の無脂乳固形分8%以上の乳飲
料については、特願平5−345296号明細書におい
て、蔗糖脂肪酸エステルを1,200ppm〜3,00
0ppm添加することにより、自動販売機による加温販
売において耐熱性菌の発芽増殖を防止できることが記載
されている。
Regarding a milk drink having a non-fat milk solid content of 8% or more in a milk drink which is not described in Japanese Patent Publication No. 57-26104, sucrose fatty acid ester is described in Japanese Patent Application No. 5-345296. 1,200 ppm to 3,000
It is described that by adding 0 ppm, germination and growth of heat-resistant bacteria can be prevented in warm sales by an automatic vending machine.

【0005】[0005]

【発明が解決しようとする課題】蔗糖脂肪酸エステルは
高価であり、また、これを多量に添加する場合はその苦
みおよびエグみのためにミルク入り低酸性飲料の味覚を
損うので、できうれば蔗糖脂肪酸エステルを添加するこ
となく自動販売機による加温販売に適した密閉容器入り
低酸性飲料を提供することが望ましい。
Sucrose fatty acid ester is expensive, and when added in a large amount, the bitterness and acridness impair the taste of a low-acidic beverage containing milk. It is desirable to provide a low-acidic beverage in a closed container suitable for hot sale by a vending machine without adding sucrose fatty acid ester.

【0006】よって、本発明の第1の目的は、蔗糖脂肪
酸エステルを添加することなく、自動販売機により加温
販売しても耐熱性菌の発芽増殖を充分に抑制することが
できる密閉容器入り低酸性飲料の製造方法を提供するこ
とにある。
Therefore, a first object of the present invention is to provide a sealed container capable of sufficiently suppressing germination and growth of heat-resistant bacteria even when heated and sold by an automatic vending machine without adding sucrose fatty acid ester. It is to provide a method for producing a low-acid beverage.

【0007】従来ミルク入り低酸性飲料内溶液をフィラ
ーから缶に充填する場合は、一般に製品の酸化防止のた
め缶のヘッドスペース内の残存酸素量を所定量以下に抑
える方法として、内容液を充填温度80℃〜90℃で缶
に充填する熱間充填法が採用されている。しかるに、本
発明者による実験の結果、この充填温度で熱間充填を行
うと、フィラーの内容液流出口に設けられたフィラーバ
ルブに乳成分が凝固付着し、この凝固した乳成分の塊が
フィラーバルブから剥離して缶内に内容液とともに入っ
た場合、レトルト加熱処理を行ってもこの乳成分の塊は
溶解せず、熱が塊の内部まで充分到達しないため耐熱性
菌が生き残る可能性があることが判った。従来のミルク
入り低酸性飲料のように蔗糖脂肪酸エステルを添加して
いる場合は、この乳成分の塊の中で生き残った耐熱性菌
は蔗糖脂肪酸エステルの制菌作用のため製品中での発芽
増殖を抑制されるので特に問題は生じないが、本発明の
上記第1の目的を達成するためミルク入り低酸性飲料に
蔗糖脂肪酸エステルを添加しない場合は、自動販売機に
よる加温販売に際して残存耐熱性菌の発芽増殖による製
品のフラットサワー状の変敗を生じるおそれがある。
Conventionally, when a can is filled with a solution in a low-acidic beverage containing milk from a filler, generally, the content liquid is filled as a method of suppressing the residual oxygen amount in the head space of the can to a predetermined amount or less in order to prevent product oxidation. A hot filling method of filling a can at a temperature of 80 ° C to 90 ° C is adopted. However, as a result of the experiment by the present inventor, when hot filling is performed at this filling temperature, the milk component is coagulated and adhered to the filler valve provided in the content liquid outlet of the filler, and the mass of the coagulated milk component is the filler. When peeled off from the valve and entered into the can together with the content liquid, the lumps of milk components do not dissolve even if a retort heat treatment is performed, and heat does not reach the inside of the lumps sufficiently, so thermostable bacteria may survive. I knew it was. When sucrose fatty acid ester is added as in conventional low-acid beverages containing milk, the thermostable bacteria that survive in the lump of milk components germinate and grow in the product due to the bacteriostatic action of sucrose fatty acid ester. However, when the sucrose fatty acid ester is not added to the low-acidic beverage containing milk in order to achieve the first object of the present invention, the residual heat resistance in the vending machine when heated is sold. May cause flat sour deterioration of the product due to germination and growth of fungi.

【0008】よって、本発明の第2の目的は、密閉容器
入り低酸性飲料を提供する場合に生じる上記問題点を解
決することにある。
Therefore, a second object of the present invention is to solve the above-mentioned problems that occur when providing a low-acidic beverage in a closed container.

【0009】[0009]

【課題を解決する手段および作用】本発明者は、上記第
1の目的を達成するため研究と実験を重ねた結果、ミル
ク入り低酸性飲料内容液の加熱殺菌処理を内容液の容器
への充填前における熱交換機による加熱処理と充填後に
おけるレトルト加熱処理の2段階加熱処理により行い、
かつこの2段階加熱処理のF0 値の合計を120以上と
することにより、製品を55℃で3週間保存しても変敗
を生じないことを発見し、本発明に到達した。
Means for Solving the Problems and Actions The present inventor has conducted research and experiment to achieve the first object, and as a result, heat sterilization treatment of a low-acid beverage content liquid containing milk was filled in a container of the content liquid. Performed by the two-stage heat treatment of the heat treatment by the heat exchanger before and the retort heat treatment after the filling,
Moreover, it was discovered that, by setting the total F 0 value of the two-step heat treatment to 120 or more, no deterioration occurs even if the product is stored at 55 ° C. for 3 weeks, and the present invention was reached.

【0010】すなわち、本発明の上記第1の目的を達成
する密閉容器入り低酸性飲料の製造方法は、蔗糖脂肪酸
エステルを含まないミルク入り低酸性飲料内容液を調合
し、均質化処理を行う前または行った後熱交換機による
加熱処理を行い、次いで内容液を容器に充填密閉した後
レトルト加熱処理を行い、熱交換機による加熱処理とレ
トルト加熱処理のF0 値の合計を120以上とすること
を特徴とする。
That is, the method for producing a low-acidic beverage contained in a closed container, which achieves the first object of the present invention, is to prepare a low-acidic beverage content liquid containing milk containing no sucrose fatty acid ester and perform a homogenizing treatment. Alternatively, after performing the heat treatment by the heat exchanger, then filling and sealing the content liquid in the container and then performing the retort heat treatment, the total F 0 value of the heat treatment by the heat exchanger and the retort heat treatment is 120 or more. Characterize.

【0011】本発明の方法によれば、F0 値120以上
の加熱殺菌を行うことにより、蔗糖脂肪酸エステル無添
加の密閉容器入り低酸性飲料を自動販売機により加温販
売しても、耐熱性菌の発芽増殖による製品の変敗を防止
することができる。しかも内容液の分離、変色、pHの
変化等製品の品質の劣化を生じることがない。
According to the method of the present invention, heat sterilization with an F 0 value of 120 or more allows heat resistance even when a low-acid beverage containing a sucrose fatty acid ester-free additive in a closed container is heated and sold by a vending machine. It is possible to prevent product deterioration due to germination and growth of bacteria. Moreover, the quality of the product does not deteriorate such as separation of the content liquid, discoloration, and change of pH.

【0012】本発明の一側面において、本発明にかかる
製造方法は、熱交換機による加熱処理のF0 値をレトル
ト加熱処理のF0 値よりも大きくすることを特徴とす
る。
[0012] In one aspect of the present invention, the production method according to the present invention, the F 0 value of heat treatment by the heat exchanger, characterized in that larger than F 0 value of retort heat treatment.

【0013】これによって、脂肪球の粒径分布は、粒子
径1μm以下の脂肪球の比率が大きくなり、長期保存に
おける内容液の分離を防止することができる。
As a result, in the particle size distribution of fat globules, the proportion of fat globules having a particle size of 1 μm or less becomes large, and separation of the content liquid during long-term storage can be prevented.

【0014】本発明の一側面において、本発明にかかる
製造方法は、熱交換機による加熱処理を2段以上に分け
て行うことを特徴とする。
In one aspect of the present invention, the manufacturing method according to the present invention is characterized in that the heat treatment by the heat exchanger is performed in two or more stages.

【0015】熱交換機による加熱処理を1段の熱交換機
により行っても、2段以上の熱交換機に分けて行って
も、殺菌効果の点では大きな差異は生じないが、1段の
熱交換機のみでF0 値100以上の加熱を行うと内容液
中の乳成分の一部が凝固して熱交換機の内壁にこびりつ
く現象が生じ易くなり、このため熱交換機のサニテーシ
ョン処理をひんぱんに行わねばならなくなり、この間製
造ラインを停止しなければならず、生産効率を低下させ
ることになる。加熱処理を2段以上の多段の熱交換機に
分けて行うことにより、各段の熱交換機における内容液
中の乳成分のこびりつきの発生を生じにくくすることが
でき、過度のサニテーション処理の実施を行う必要がな
く、生産効率の低下を防止することができる。
Whether the heat treatment by the heat exchanger is carried out by a one-stage heat exchanger or by dividing it into two or more stages, there is no great difference in the sterilizing effect, but only the one-stage heat exchanger is used. When the F 0 value of 100 or more is heated in the above, a part of the milk component in the content liquid is solidified and the phenomenon of sticking to the inner wall of the heat exchanger easily occurs. Therefore, the sanitation process of the heat exchanger must be frequently performed. The production line must be stopped during this period, which reduces production efficiency. By dividing the heat treatment into two or more multi-stage heat exchangers, it is possible to prevent the milk component in the content liquid from sticking to the heat exchangers in each stage, and to perform excessive sanitation treatment. It is not necessary to carry out, and it is possible to prevent a decrease in production efficiency.

【0016】本発明の上記第2の目的を達成する密閉容
器入り低酸性飲料の製造方法は、フィラーにより内容液
を容器に充填し、その際の充填温度を35℃以下とする
ことを特徴とする。
The method for producing a low-acidic beverage contained in a closed container, which achieves the second object of the present invention, is characterized in that the container is filled with the content liquid and the filling temperature at that time is set to 35 ° C. or lower. To do.

【0017】充填温度を35℃以下とすることにより、
フィラーバルブに乳成分が凝固付着しその塊が容器内部
に混入することがなくなり、したがって、この乳成分の
塊の中に耐熱性菌が生存して自動販売機による加温販売
中に発芽増殖し製品の変敗を生じることを防止すること
ができる。
By setting the filling temperature to 35 ° C. or lower,
The milk component does not coagulate and adhere to the filler valve and the lump does not mix inside the container.Therefore, heat-resistant bacteria survive in this lump of milk component and germinate and proliferate during warm sale by the vending machine. It is possible to prevent the deterioration of the product.

【0018】本発明の他の側面において、本発明にかか
る製造方法は、充填温度35℃以下で内容液を容器に充
填した後容器を密閉する前に容器内の空気を、水蒸気ま
たは窒素ガスと水蒸気の混合ガスにより置換することを
特徴とする。
In another aspect of the present invention, in the manufacturing method according to the present invention, the air in the container is filled with water vapor or nitrogen gas after filling the container with the content liquid at a filling temperature of 35 ° C. or less and before sealing the container. It is characterized in that it is replaced by a mixed gas of steam.

【0019】これによって、ヘッドスペース内の残存酸
素量を所定量以下に抑えることができ、充填温度が低い
ために生じる酸化防止の不充分性を補うことができる。
また、真空度を高くすることも可能であり、レトルト殺
菌の際に、ヘッドスペース内の気体の熱膨張によるバッ
クリング(缶の膨出変形)の発生も防止することができ
る。
As a result, the amount of oxygen remaining in the head space can be suppressed to a predetermined amount or less, and the insufficient oxidation prevention caused by the low filling temperature can be compensated.
It is also possible to increase the degree of vacuum, and it is possible to prevent the occurrence of buckling (bulging deformation of the can) due to thermal expansion of the gas in the head space during retort sterilization.

【0020】容器内の空気を窒素ガスと水蒸気の混合ガ
スにより置換するには、たとえば特公昭63−5024
9号公報に記載された方法を用い、所定の酸素量、真空
度になるように調整する。
To replace the air in the container with a mixed gas of nitrogen gas and water vapor, for example, Japanese Patent Publication No. 63-5024.
Using the method described in Japanese Patent No. 9, adjustment is made so that the amount of oxygen and the degree of vacuum are predetermined.

【0021】本発明の方法は、コーヒー牛乳ばかりでな
く、ミルクココア、ミルクコーヒー、カフェオーレ等の
ミルク入り低酸性飲料に広く適用することができる。
The method of the present invention can be widely applied not only to coffee milk, but also to low-acidic beverages containing milk such as milk cocoa, milk coffee and cafe aure.

【0022】熱交換機としては、プレート式、チューブ
式等レトルト前の内容液の第一次加熱に使用可能なもの
であればいずれの型の熱交換機も使用可能である。
As the heat exchanger, any type of heat exchanger such as a plate type or a tube type can be used as long as it can be used for the primary heating of the content liquid before retort.

【0023】[0023]

【実施例】以下本発明の実施例について説明する。本発
明にかかる製造方法において、蔗糖脂肪酸エステルを添
加することなく自動販売機により加温販売しても耐熱性
菌の発芽増殖を充分に抑制することができるF0 値を見
出すため、本発明者は、試験対象耐熱性菌としてC.ther
mohydrosulfuricum、 C.thermoaceticumを使用して、以
下の実施例に示すように、加熱による耐熱性菌の発芽増
殖抑制試験(実施例1〜5)を行った。
EXAMPLES Examples of the present invention will be described below. In the production method according to the present invention, the inventors of the present invention have found an F 0 value that can sufficiently suppress germination and growth of thermostable bacteria even when heated and sold by an automatic vending machine without adding sucrose fatty acid ester. C.ther as a thermostable bacterium to be tested
Using mohydrosulfuricum and C. thermoaceticum, a germination and growth inhibition test of heat-resistant bacteria by heating (Examples 1 to 5) was carried out as shown in the following Examples.

【0024】実施例1 次の成分組成のコーヒー牛乳モデル液を調合した。 Example 1 A coffee milk model liquid having the following composition was prepared.

【0025】 市販牛乳 69.3% グラニュー糖 3.0% 脱脂粉乳 2.4% 粉末コーヒー 0.4% 重曹 0.07% 活性炭処理水 24.83% このモデル液をホモジナイザーにより250kg/cm
2 で均質化処理を行った後C.thermohydrosulfuricum を
1.6×104 /mlの濃度になるように接種した。次
いでモデル液を各試験区6本ずつ24の試験区において
TDTチューブに2mlずつ充填し溶封した後、2段の
オイルバスにより各段のF0 値を0〜120の間で種々
変えて加熱した。これら試験区のチューブを55℃で3
週間保存した後の供試チューブ(6本)中の変敗チュー
ブの数を表1に示す。
Commercial milk 69.3% Granulated sugar 3.0% Non-fat dry milk 2.4% Powdered coffee 0.4% Baking soda 0.07% Activated carbon treated water 24.83% This model liquid was 250 kg / cm by a homogenizer.
After homogenization treatment at 2 , C. thermohydrosulfuricum was inoculated to a concentration of 1.6 × 10 4 / ml. Then, in each of the 24 test sections, the model solution was filled with 2 ml of TDT tube in each of the 24 test sections, and sealed, and then heated by varying the F 0 value of each step from 0 to 120 by a two-step oil bath. did. Tubes of these test plots at 55 ℃ for 3
Table 1 shows the number of deteriorated tubes in the test tubes (6 tubes) after storage for a week.

【0026】[0026]

【表1】 [Table 1]

【0027】実施例2 耐熱性菌の濃度を8.4×101 /mlとした以外は実
施例1と同様の方法により2段加熱による試験を行っ
た。その結果を表2に示す。
Example 2 A two-stage heating test was conducted in the same manner as in Example 1 except that the concentration of thermostable bacteria was changed to 8.4 × 10 1 / ml. The results are shown in Table 2.

【0028】[0028]

【表2】 [Table 2]

【0029】実施例3 加熱を3段のオイルバスに分けて行い、また、耐熱性菌
の濃度を1.3×103 /mlとした以外は実施例1と
同様の方法により試験を行った。その結果を表3に示
す。
Example 3 A test was conducted in the same manner as in Example 1 except that the heating was divided into three oil baths and the concentration of thermostable bacteria was 1.3 × 10 3 / ml. . Table 3 shows the results.

【0030】[0030]

【表3】 [Table 3]

【0031】実施例4 耐熱性菌の濃度を4.9×102 /mlとした以外は実
施例3と同様の方法により3段加熱による試験を行っ
た。その結果を表4に示す。
Example 4 A test was conducted by heating in three steps in the same manner as in Example 3 except that the concentration of thermostable bacteria was 4.9 × 10 2 / ml. The results are shown in Table 4.

【0032】[0032]

【表4】 [Table 4]

【0033】実施例5 各段のF0 値を0〜130の間で変化させ,そして、試
験対象耐熱性菌としてC.thermoaceticum 1.3×10
3 /mlを使用した以外は実施例4と同様の方法により
3段加熱による試験を行った。その結果を表5に示す。
Example 5 The F 0 value of each stage was changed from 0 to 130, and C. thermoaceticum 1.3 × 10 was selected as the thermostable bacterium to be tested.
A test by three-stage heating was conducted in the same manner as in Example 4 except that 3 / ml was used. The results are shown in Table 5.

【0034】[0034]

【表5】 [Table 5]

【0035】上記実施例1〜5の試験の結果、加熱を1
段、2段または3段で行うとを問わず、F0 値の合計が
120以上であれば、55℃で3週間保存してもモデル
液の変敗は生じないことが判った。
As a result of the tests of the above Examples 1 to 5, the heating was 1
It was found that the model solution did not deteriorate even if it was stored at 55 ° C. for 3 weeks as long as the total F 0 value was 120 or more, regardless of whether it was performed in two steps, two steps or three steps.

【0036】実施例6 次に、表6に示すように、実施例1と同一組成のコーヒ
ー牛乳モデル液についてF0 値の合計を役120とし、
1段の熱交換機によるF0 値を75.8、レトルトによ
るF0 値を44.5として加熱した場合(マーク1)、
熱交換機による加熱を2段に分けてそれぞれF0 値50
ずつ、レトルトによるF0 値を19.8として加熱した
場合(マーク2)、および熱交換機による加熱を行わず
レトルトのみでF0 値119.7の加熱を行った場合
(マーク3)における脂肪球の粒子径分布、pHおよび
色の変化を測定した。なお各モデル液はレトルト前にホ
モジナイザーにより250kg/cm2 で均質化処理を
行い、200g缶に充填してレトルト加熱を行った。
Example 6 Next, as shown in Table 6, with respect to the coffee milk model liquid having the same composition as in Example 1, the total of F 0 values was set to 120.
When heating is performed with the F 0 value of the one-stage heat exchanger set to 75.8 and the F 0 value of the retort set to 44.5 (mark 1),
The heating by the heat exchanger is divided into two stages and each has an F 0 value of 50.
Fat globules when heated with a F 0 value of 19.8 (mark 2) by the retort (mark 2) and when heating with a F 0 value of 119.7 only by the retort without heating by the heat exchanger (mark 3) The particle size distribution, pH, and color change were measured. Each model solution was homogenized with a homogenizer at 250 kg / cm 2 before retort, filled in a 200 g can, and heated in a retort.

【0037】[0037]

【表6】 [Table 6]

【0038】脂肪球の中1μm以下の粒子径の粒子の役
割(%)をレトルト直後、55℃で1週間保存後、55
℃で2週間保存後にそれぞれ測定した結果を表7に示
す。
The role (%) of particles having a particle size of 1 μm or less in fat globules was stored immediately after retort and after storage at 55 ° C. for 1 week,
Table 7 shows the results of each measurement after storage at 2 ° C for 2 weeks.

【0039】[0039]

【表7】 [Table 7]

【0040】粒子径1μm以下の粒子が90%未満では
時間経過とともに液中の乳成分の分離が生じ易く好まし
くない。表7の測定結果は、F0 値の合計は同じでも、
レトルト単独による加熱よりも、熱交換機とレトルトに
分けて加熱を行った方が1μm以下の粒子の割合は大き
く、また、熱交換機による加熱を1段で行うよりも2段
に分けて行う方が1μm以下の粒子の割合は大きいこと
を示している。また次に、レトルト直後、55℃で1週
間保存後、55℃で2週間保存後にそれぞれ測定したモ
デル液のpHを表8に示す。
If the proportion of particles having a particle size of 1 μm or less is less than 90%, the milk components in the liquid tend to separate with the passage of time, which is not preferable. The measurement results in Table 7 show that the total F 0 values are the same,
The ratio of particles with a size of 1 μm or less is larger when heating is performed separately in the heat exchanger and the retort than when heating by the retort alone, and heating in the heat exchanger is performed in two stages rather than in one stage. It is shown that the proportion of particles of 1 μm or less is large. Table 8 shows the pH values of the model solutions measured immediately after retort, after storage at 55 ° C for 1 week, and after storage at 55 ° C for 2 weeks.

【0041】[0041]

【表8】 [Table 8]

【0042】コーヒー牛乳等のミルク入り低酸性飲料に
おいては、pHが6.2以下では風味が落ちることが考
えられる。表8の結果から、F0 値は同じでもレトルト
のみによる加熱によるマーク3の場合はpHは6.1で
あり、風味の点では好ましくなく、熱交換機とレトルト
に分けて加熱を行った方が良好な風味を維持できること
が判った。
In a low-acidic beverage containing milk such as coffee milk, it is considered that the flavor is deteriorated when the pH is 6.2 or less. From the results shown in Table 8, even if the F 0 value is the same, in the case of Mark 3 by heating with only the retort, the pH is 6.1, which is not preferable in terms of flavor, and it is better to heat the heat exchanger separately from the retort. It has been found that a good flavor can be maintained.

【0043】また、レトルト直後の表6のマーク1のモ
デル液の色を標準として各マークについてレトルト直
後、55℃で1週間保存後、55℃で2週間保存後にそ
れぞれ行ったモデル液の色差測定の結果を表9に示す。
Color difference measurement of the model liquid was carried out for each mark immediately after retort, immediately after retort, after storage at 55 ° C. for 1 week, and after storage at 55 ° C. for 2 weeks, using the color of the model liquid immediately after the retort as a standard. The results are shown in Table 9.

【0044】[0044]

【表9】 [Table 9]

【0045】また、各マークのモデル液のレトルト直後
の色を標準として各マークについて55℃で1週間保存
後、55℃で2週間保存後に行ったモデル液の色差測定
の結果を表10に示す。
Table 10 shows the results of the color difference measurement of the model liquids after each mark was stored at 55 ° C for 1 week and after being stored at 55 ° C for 2 weeks, with the color of each mark immediately after the retort as a standard. .

【0046】[0046]

【表10】 [Table 10]

【0047】表9および表10の結果から、マーク3の
場合は色差が大きく(赤茶けた色に変色する)、F0
120をレトルト加熱のみにより実現しようとすると内
容液の変色を防ぐことができず、色の点で満足できる製
品が作れないことが判った。
From the results of Table 9 and Table 10, in the case of mark 3, the color difference is large (discoloring to reddish brown), and if the F 0 value of 120 is attempted to be achieved only by retort heating, discoloration of the content liquid can be prevented. It turned out that it was not possible to make a product that was satisfactory in terms of color.

【0048】実施例7 表11に示すように、実施例1と同一組成のコーヒー牛
乳モデル液についてF0 値の合計を約120とし、1段
ないし3段の熱交換機による合計F0 値を約100、レ
トルトによるF0 値を約20として加熱した場合(マー
ク4〜6)および3段の熱交換機によるF0 値を約11
5、レトルトによるF0 値を約5として加熱した場合
(マーク7,8)における脂肪球の粒子径分布、pHお
よび色の変化を測定した。なお各モデル液はレトルト前
にホモジナイザーにより250kg/cm2 で均質化処
理を行い、200g缶に充填してレトルト加熱を行っ
た。
[0048] As shown in Example 7 Table 11, the F 0 value total of about 120 for the coffee milk model solution having the same composition as Example 1, about the total F 0 value by one stage to three-stage heat exchangers 100, when the F 0 value by the retort was set to about 20 (marks 4 to 6) and the F 0 value by the three-stage heat exchanger was about 11
5, the F 0 value by the retort was set to about 5, and the particle size distribution, pH and color change of fat globules when heated (marks 7 and 8) were measured. Each model solution was homogenized with a homogenizer at 250 kg / cm 2 before retort, filled in a 200 g can, and heated in a retort.

【0049】[0049]

【表11】 [Table 11]

【0050】脂肪球の中1μm以下の粒子径の粒子の割
合(%)をレトルト直後、55℃で1週間保存後、55
℃で2週間保存後に測定した結果を表12に示す。
The proportion (%) of particles having a particle size of 1 μm or less in fat globules was stored immediately after retort and stored at 55 ° C. for 1 week.
Table 12 shows the results of measurement after storage at 2 ° C for 2 weeks.

【0051】[0051]

【表12】 [Table 12]

【0052】測定結果はいずれも粒子径1μm以上の粒
子が95%以上を占め満足すべきものであることを示し
ている。特に熱交換機によるF0 値を約115、レトル
トによるF0 値を約5としたマーク7,8の場合は1μ
m以下の粒子径の粒子が98%を占め、熱交換機による
加熱処理のF0 値をレトルト加熱処理のF0 値よりも大
きくすることが有利であることが判った。
The measurement results show that particles having a particle size of 1 μm or more account for 95% or more and should be satisfied. Particularly, in the case of the marks 7 and 8 in which the F 0 value by the heat exchanger is about 115 and the F 0 value by the retort is about 5, 1 μm
m or less in particle size particles accounted for 98%, the F 0 value of heat treatment by the heat exchanger be made larger than the F 0 value of retort heat treatment was found to be advantageous.

【0053】次に、レトルト直後、55℃で1週間保存
後、55℃で2週間保存後にそれぞれ測定したpHを表
13に示す。
Table 13 shows the pH values measured immediately after retort, after storage at 55 ° C. for 1 week and after storage at 55 ° C. for 2 weeks.

【0054】[0054]

【表13】 [Table 13]

【0055】表13の結果は、55℃で2週間保存後の
pHは6.3以上で満足すべきものであることを示して
いる。また、レトルト直後の表11のマーク4のモデル
液の色を標準としてマーク4〜8についてレトルト直
後、55℃で1週間保存後、55℃で2週間保存後にそ
れぞれ行ったモデル液の色差測定の結果を表14に示
す。
The results in Table 13 show that the pH after storage at 55 ° C. for 2 weeks was 6.3 or more, which was satisfactory. In addition, with respect to the marks 4 to 8 using the color of the model liquid of mark 4 in Table 11 immediately after the retort as a standard, the color difference measurement of the model liquid was performed immediately after the retort, after storing at 55 ° C for 1 week, and after storing at 55 ° C for 2 weeks. The results are shown in Table 14.

【0056】[0056]

【表14】 [Table 14]

【0057】また、各マーク4〜8のモデル液のレトル
ト直後の色を標準として、各マークについて55℃で1
週間保存後、55℃で2週間保存後に行ったモデル液の
色差測定の結果を表15に示す。
Further, the color of each of the marks 4 to 8 immediately after the retort of the model liquid was used as a standard, and each mark had a color of 1 at 55 ° C.
Table 15 shows the results of the color difference measurement of the model liquid, which was carried out after storage for a week and at 55 ° C. for 2 weeks.

【0058】[0058]

【表15】 [Table 15]

【0059】表14および表15の結果は、熱交換機に
よる加熱とレトルト加熱を併用する場合大きな色の変化
は起らず満足すべき結果が得られることを示している。
The results in Tables 14 and 15 show that when the heating by the heat exchanger and the retort heating are used in combination, a large color change does not occur and a satisfactory result is obtained.

【0060】実施例8 フィラーバルブに凝固付着した乳成分の塊の中に生存す
る耐熱性菌の増殖可能性を調べるため次の試験を行っ
た。
Example 8 The following test was conducted in order to investigate the growth potential of thermostable bacteria that survive in the mass of milk components coagulated and adhered to the filler valve.

【0061】試験1 耐熱性菌B.stearothermophilusを市販のコーヒー牛乳に
添加し37℃または110℃のいずれかの乾燥温度で乾
燥して固形物とした。次にこの固形物を取りTDTチュ
ーブに0.01〜0.04g入れた後市販のコーヒー牛
乳を各チューブに2ml充填し溶封した後、121.1
℃で所定時間加熱した後、55℃で3週間保存後の変敗
チューブ数を調べた。その結果を表16に示す。
Test 1 The heat-resistant bacterium B. stearothermophilus was added to commercially available coffee milk and dried at a drying temperature of either 37 ° C. or 110 ° C. to give a solid. Next, 0.01 to 0.04 g of this solid substance was put into a TDT tube, and then 2 ml of commercially available coffee milk was filled in each tube and the mixture was sealed.
After heating at 0 ° C for a predetermined time, the number of deteriorated tubes after storage at 55 ° C for 3 weeks was examined. The results are shown in Table 16.

【0062】[0062]

【表16】 [Table 16]

【0063】37℃で乾燥固化した塊は121.1℃で
溶解したが110℃で乾燥固化した塊は121.1℃で
溶解しなかった。そして塊が溶解したものについては1
21.1℃、3分以上の加熱により変敗チューブは発生
しなかったが、塊が溶解しなかったものについては12
1.1℃、20分の加熱によっても変敗チューブが発生
した。この結果からコーヒー牛乳中に乳成分の塊が溶解
せずに残ると耐熱性菌が生残り発芽増殖することが判っ
た。
The lump dried and solidified at 37 ° C. dissolved at 121.1 ° C., but the lump dried and solidified at 110 ° C. did not dissolve at 121.1 ° C. And 1 for the one that the lump melted
No spoiled tube was generated by heating at 21.1 ° C for 3 minutes or more, but 12 if the lump did not dissolve
A deterioration tube was also generated by heating at 1.1 ° C. for 20 minutes. From these results, it was found that the thermostable bacteria survived and germinated and propagated when the lumps of milk components remained in the coffee milk without being dissolved.

【0064】次に上記菌種を用いて、芽胞を塊にしない
で均一に分散させて行う通常の耐熱性試験を行った。す
なわち、上記耐熱性菌を1.4×105 個/mlの濃度
になるように市販のコーヒー牛乳に添加し、このコーヒ
ー牛乳をTDTチューブに2ml充填し溶封した後、1
21.1℃で所定時間加熱した後55℃で3週間保存後
の変敗チューブ数を調べた。その結果を表17に示す。
Next, using the above-mentioned bacterial species, a usual heat resistance test was carried out in which the spores were not dispersed but were uniformly dispersed. That is, the above heat-resistant bacterium was added to commercially available coffee milk to a concentration of 1.4 × 10 5 cells / ml, 2 ml of this coffee milk was filled in a TDT tube, and the mixture was sealed.
After heating at 21.1 ° C. for a predetermined time and storing at 55 ° C. for 3 weeks, the number of deteriorated tubes was examined. The results are shown in Table 17.

【0065】[0065]

【表17】 [Table 17]

【0066】表17の結果から、塊が存在しない場合は
121.1℃、4分以上の加熱により変敗チューブは発
生しないことが判った。
From the results shown in Table 17, it was found that in the absence of lumps, a septic tube was not generated by heating at 121.1 ° C. for 4 minutes or longer.

【0067】試験2 缶詰を使用して試験1と同様の試験を行った。B.stearo
thermophilusを市販のコーヒー牛乳に添加し200g缶
の空缶のクレパス部に添加し95℃、30分の加熱によ
り乾燥固化させた。次に缶に市販のコーヒー牛乳を充填
温度90℃で充填し、レトルトにより所定の殺菌を行っ
た後55℃で3週間保存した後の変敗缶の数を調べた。
また対照として、空缶のクレパス部に塊を作成しないで
市販のコーヒー牛乳を充填した直後に同一菌種の芽胞の
懸濁液を添加してその後同様の処理をした缶詰も作成し
て変敗缶の有無を調べた。その結果を表18に示す。
Test 2 A test similar to Test 1 was conducted using canned food. B.stearo
Thermophilus was added to commercially available coffee milk, added to the crepe portion of an empty can of 200 g, and dried and solidified by heating at 95 ° C. for 30 minutes. Next, the cans were filled with commercially available coffee milk at a filling temperature of 90 ° C., sterilized by a retort, and stored at 55 ° C. for 3 weeks.
As a control, a spore suspension of the same bacterial species was added immediately after filling commercially available coffee milk without making lumps in the crepe part of an empty can, and then a similar treatment was also made to make spoilage. I checked the presence of a can. The results are shown in Table 18.

【0068】[0068]

【表18】 [Table 18]

【0069】表18の結果から、缶詰においても塊が存
在しない缶については121.1℃、5分以上の加熱に
より変敗缶は発生しなかったが、塊の存在する缶につい
ては変敗缶が生じることが判った。
From the results shown in Table 18, the cans which do not have lumps even when they are canned did not cause deterioration of the cans by heating at 121.1 ° C. for 5 minutes or more, but the cans having lumps caused deterioration of the cans. Was found to occur.

【0070】上記試験1、試験2の結果、乳成分の塊の
中に耐熱性菌の芽胞が塊となって存在すると菌の耐熱性
が増大し変敗の可能性が増大することが判った。また、
加熱処理時に内容液中に乳成分の塊が溶解しているか否
かが重要であることが判った。
As a result of Tests 1 and 2 described above, it was found that the presence of spores of heat-resistant bacteria in a mass in the mass of milk components increases the heat resistance of the bacteria and increases the possibility of spoilage. . Also,
It was found that it is important whether or not the lumps of milk components are dissolved in the content liquid during the heat treatment.

【0071】実施例9 実際のフィラーを想定して、フィラーバルブにおける乳
成分の凝固付着について試験機を用いてシミュレート試
験を行った。この試験に使用した試験機は図1に模式的
に示すもので、原液タンク1に貯蔵される原液はポンプ
2により汲み出されオイルバス3に供給され加熱され
る。次に加熱された原液は配管7を介して上部に配置さ
れた供給タンク4に供給される。この供給タンク4の下
部には可変モータ6の動作により開閉される公知の構造
のフィラーバルブ5が設けられており、原液はフィラー
バルブ5から、冷却タンク7に供給され冷却された後原
液タンク1に戻される。こうして上記の工程が繰返され
原液は系内を循環して加熱、冷却が繰返される。
Example 9 Assuming an actual filler, a simulated test was conducted using a tester for coagulation and adhesion of milk components in a filler valve. The test machine used for this test is shown schematically in FIG. 1, and the stock solution stored in the stock solution tank 1 is pumped out by a pump 2 and supplied to an oil bath 3 to be heated. Next, the heated stock solution is supplied to the supply tank 4 arranged at the upper part through the pipe 7. A filler valve 5 having a known structure that is opened and closed by the operation of the variable motor 6 is provided below the supply tank 4, and the stock solution is supplied from the filler valve 5 to the cooling tank 7 and then cooled. Returned to. In this way, the above steps are repeated, and the stock solution is circulated in the system to repeat heating and cooling.

【0072】市販のコーヒー牛乳にB.stearothermophil
usを2.4×104 個/mlの濃度になるように添加し
て、この液を上記試験機内で循環させ、加熱温度を種々
変えてフィラーバルブ5を開閉することによりフィラー
バルブ5内における乳成分の凝固付着の有無を調べた。
次にその付着物をTDTチューブに取り市販コーヒー牛
乳2mlを充填して溶封し、オイルバスにより加熱処理
を施した後55℃で3週間保存後の変敗チューブの数を
調べた。フィラーバルブにおける循環温度(充填温
度)、フィラーバルブにおける乳成分付着の有無、変販
缶数および加熱処理時における塊の溶解有無を表19に
示す。
Commercially available coffee milk with B. stearothermophil
Add us to a concentration of 2.4 × 10 4 cells / ml, circulate this solution in the above tester, and change the heating temperature variously to open / close the filler valve 5 so that the filler valve 5 The presence or absence of coagulation and adhesion of milk components was examined.
Next, the attached matter was taken into a TDT tube, 2 ml of commercially available coffee milk was filled therein, and the mixture was sealed. After heat treatment with an oil bath, the number of spoiled tubes after storage at 55 ° C for 3 weeks was examined. Table 19 shows the circulation temperature (filling temperature) in the filler valve, the presence / absence of milk component adhesion in the filler valve, the number of variable sales cans, and the presence / absence of lump dissolution during heat treatment.

【0073】[0073]

【表19】 [Table 19]

【0074】表19の結果から、充填温度35℃ではフ
ィラーバルブ内での乳成分の付着は僅かに生じたが、1
21.1℃、1分以上の加熱により変敗チューブは生じ
なかった。また、充填温度30℃では乳成分の付着はま
ったく生じなかった。この事実からミルク入り低酸性飲
料の充填温度を35℃以下、好ましくは30℃以下とす
ることにより、フィラーバルブに乳成分が凝固付着する
ことがなく、自動販売機による加温販売中に耐熱性菌が
発芽増殖するおそれがないことが判った。
From the results shown in Table 19, when the filling temperature was 35 ° C., the adhesion of the milk component slightly occurred in the filler valve.
No deterioration tube was formed by heating at 21.1 ° C for 1 minute or more. Further, at the filling temperature of 30 ° C., no adhesion of milk components occurred. From this fact, by setting the filling temperature of the low-acidic beverage containing milk to 35 ° C. or lower, preferably 30 ° C. or lower, the milk component does not coagulate and adhere to the filler valve, and the heat resistance during heating and sales by the vending machine is improved. It was found that there is no risk of germs growing and growing.

【0075】[0075]

【発明の効果】以上述べたように、本発明の方法によれ
ば、蔗糖脂肪酸エステルを含まないミルク入り低酸性飲
料内容液を調合し、均質化処理を行う前または行った後
熱交換機による加熱処理を行い、次いで内容液を容器に
充填密閉した後レトルト加熱処理を行い、熱交換機によ
る加熱処理とレトルト加熱処理のF0 値の合計を120
以上とすることにより、蔗糖脂肪酸エステル無添加の密
閉容器入りミルク入り低酸性飲料を自動販売機により加
温販売しても、耐熱性菌の発芽増殖による製品の変敗を
防止することができる。しかも内容液の分離、変色、p
Hの変化等製品の品質の劣化を生じることがない。
As described above, according to the method of the present invention, a low acid beverage content liquid containing milk containing no sucrose fatty acid ester is prepared and heated by a heat exchanger before or after homogenization treatment. Then, the container is filled with the content liquid and sealed, and then the retort heat treatment is performed, and the total F 0 value of the heat treatment by the heat exchanger and the retort heat treatment is 120.
By the above, even if a low-acidic beverage containing milk in a closed container without addition of sucrose fatty acid ester is heated and sold by a vending machine, deterioration of the product due to germination and growth of heat-resistant bacteria can be prevented. Moreover, separation of content liquid, discoloration, p
There is no deterioration of product quality such as H change.

【0076】また、本発明の方法によれば、熱交換機に
よる加熱処理のF0 値をレトルト加熱処理のF0 値より
も大きくすることにより、脂肪球の粒径分布は、粒子径
1μm以下の脂肪球の比率が大きくなり、長期保存にお
ける内容液の分離を防止することができる。
[0076] Further, according to the method of the present invention, by the F 0 value of heat treatment by a heat exchanger larger than the F 0 value of retort heat treatment, the particle size distribution of the fat globules, the particle size not greater than 1μm The ratio of fat globules becomes large, and the separation of the content liquid during long-term storage can be prevented.

【0077】また、本発明の方法によれば、熱交換機に
よる加熱処理を2段以上に分けて行うことにより、各段
の熱交換機における内容液中の乳成分のこびりつきの発
生を防止することができ、過度のサニテーションの実施
を行う必要がなく、生産効率の低下を防止することがで
きる。
According to the method of the present invention, the heat treatment by the heat exchanger is performed in two or more stages, so that the milk component in the content liquid in the heat exchanger at each stage can be prevented from sticking. Therefore, it is not necessary to perform excessive sanitation, and it is possible to prevent a decrease in production efficiency.

【0078】また、本発明の方法によれば、フィラーに
より内容液を容器に充填し、その際の充填温度を35℃
以下とすることにより、フィラーバルブに乳成分が凝固
付着しその塊が容器内部に混入することがなくなり、し
たがって、この乳成分の塊の中に耐熱性菌が生存して自
動販売機による加温販売中に発芽増殖し製品の変敗を生
じることを防止することができる。
Further, according to the method of the present invention, the content liquid is filled in the container with the filler, and the filling temperature at that time is 35 ° C.
By the following, the milk components will not coagulate and adhere to the filler valve and the lumps will not be mixed inside the container.Therefore, the heat-resistant bacteria will survive in the lumps of the dairy components and will be heated by the vending machine. It is possible to prevent germination and multiplication during the sale and deterioration of the product.

【0079】また、本発明の方法によれば、充填温度3
5℃以下で内容液を容器に充填した後容器を密閉する前
に容器内の空気を、水蒸気または窒素ガスと水蒸気の混
合ガスにより置換することにより、ヘッドスペース内の
残存酸素量を所定量以下に抑えることができ、充填温度
が低いために生じる酸化防止の不充分性を補うことがで
きる。また、真空度を高くすることも可能であり、レト
ルト殺菌の際に、ヘッドスペース内の気体の熱膨張によ
るバックリング(缶の膨出変形)の発生も防止すること
ができる。
According to the method of the present invention, the filling temperature is 3
After filling the container with the content liquid at 5 ° C or less and before sealing the container, the air in the container is replaced with steam or a mixed gas of nitrogen gas and steam to reduce the residual oxygen amount in the headspace to a predetermined amount or less. It is possible to suppress the above, and it is possible to compensate for the insufficient oxidation prevention caused by the low filling temperature. It is also possible to increase the degree of vacuum, and it is possible to prevent the occurrence of buckling (bulging deformation of the can) due to thermal expansion of the gas in the head space during retort sterilization.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の方法を実施するための試験機を模式的
に示す図である。
FIG. 1 is a diagram schematically showing a testing machine for carrying out the method of the present invention.

─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成6年10月27日[Submission date] October 27, 1994

【手続補正1】[Procedure Amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0007[Correction target item name] 0007

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0007】従来ミルク入り低酸性飲料内液をフィラ
ーから缶に充填する場合は、一般に製品の酸化防止のた
め缶のヘッドスペース内の残存酸素量を所定量以下に抑
える方法として、内容液を充填温度80℃〜90℃で缶
に充填する熱間充填法が採用されている。しかるに、本
発明者による実験の結果、この充填温度で熱間充填を行
うと、フィラーの内容液流出口に設けられたフィラーバ
ルブに乳成分が凝固付着し、この凝固した乳成分の塊が
フィラーバルブから剥離して缶内に内容液とともに入っ
た場合、レトルト加熱処理を行ってもこの乳成分の塊は
溶解せず、熱が塊の内部まで充分到達しないため耐熱性
菌が生き残る可能性があることが判った。従来のミルク
入り低酸性飲料のように蔗糖脂肪酸エステルを添加して
いる場合は、この乳成分の塊の中で生き残った耐熱性菌
は蔗糖脂肪酸エステルの制菌作用のため製品中での発芽
増殖を抑制されるので特に問題は生じないが、本発明の
上記第1の目的を達成するためミルク入り低酸性飲料に
蔗糖脂肪酸エステルを添加しない場合は、自動販売機に
よる加温販売に際して残存耐熱性菌の発芽増殖による製
品のフラットサワー状の変敗を生じるおそれがある。
[0007] When filling a conventional milk low acid beverages Description liquid from filler can, as a method of generally suppressing the residual oxygen content in the headspace of the can prevent oxidation of the product below a predetermined amount, the content liquid A hot filling method of filling a can at a filling temperature of 80 ° C to 90 ° C is adopted. However, as a result of the experiment by the present inventor, when hot filling is performed at this filling temperature, the milk component is coagulated and adhered to the filler valve provided in the content liquid outlet of the filler, and the mass of the coagulated milk component is the filler. When peeled off from the valve and entered into the can together with the content liquid, the lumps of milk components do not dissolve even if a retort heat treatment is performed, and heat does not reach the inside of the lumps sufficiently, so thermostable bacteria may survive. I knew it was. When sucrose fatty acid ester is added as in conventional low-acid beverages containing milk, the thermostable bacteria that survive in the lump of milk components germinate and grow in the product due to the bacteriostatic action of sucrose fatty acid ester. However, when the sucrose fatty acid ester is not added to the low-acidic beverage containing milk in order to achieve the first object of the present invention, the residual heat resistance in the vending machine when heated is sold. May cause flat sour deterioration of the product due to germination and growth of fungi.

【手続補正2】[Procedure Amendment 2]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0036[Correction target item name] 0036

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0036】実施例6 次に、表6に示すように、実施例1と同一組成のコーヒ
ー牛乳モデル液についてF値の合計を120とし、
1段の熱交換機によるF値を75.8、レトルトによ
るF値を44.5として加熱した場合(マーク1)、
熱交換機による加熱を2段に分けてそれぞれF値50
ずつ、レトルトによるF値を19.8として加熱した
場合(マーク2)、および熱交換機による加熱を行わず
レトルトのみでF値119.7の加熱を行った場合
(マーク3)における脂肪球の粒子径分布、pHおよび
色の変化を測定した。なお各モデル液はレトルト前にホ
モジナイザーにより250kg/cmで均質化処理を
行い、200g缶に充填してレトルト加熱を行った。
Example 6 Next, as shown in Table 6, the total F 0 value of the coffee milk model liquid having the same composition as in Example 1 was set to about 120,
When heating is performed with the F 0 value by the one-stage heat exchanger being 75.8 and the F 0 value by the retort being 44.5 (mark 1),
The heating by the heat exchanger is divided into two stages and each has a F 0 value of 50.
Fat globules when heated with the F 0 value of 19.8 (mark 2) by the retort (mark 2) and when heating with the F 0 value of 119.7 only by the retort without heating by the heat exchanger (mark 3) The particle size distribution, pH, and color change were measured. Before the retort, each model liquid was homogenized with a homogenizer at 250 kg / cm 2 , filled in a 200 g can and heated in a retort.

【手続補正3】[Procedure 3]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】0072[Name of item to be corrected] 0072

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【0072】市販のコーヒー牛乳にB.stearot
hermophilusを2.4×10個/mlの濃
度になるように添加して、この液を上記試験機内で循環
させ、加熱温度を種々変えてフィラーバルブ5を開閉す
ることによりフィラーバルブ5内における乳成分の凝固
付着の有無を調べた。次にその付着物をTDTチューブ
に取り市販コーヒー牛乳2mlを充填して溶封し、オイ
ルバスにより加熱処理を施した後55℃で3週間保存後
の変敗チューブの数を調べた。フィラーバルブにおける
循環温度(充填温度)、フィラーバルブにおける乳成分
付着の有無、変敗チューブ数および加熱処理時における
塊の溶解有無を表19に示す。
Commercially available coffee milk with B.I. stearot
Thermophilus was added to a concentration of 2.4 × 10 4 cells / ml, this solution was circulated in the tester, and the filler valve 5 was opened / closed by variously changing the heating temperature to open / close the filler valve 5. The presence or absence of coagulation and adhesion of milk components was examined. Next, the attached matter was taken in a TDT tube, 2 ml of commercially available coffee milk was filled therein, the mixture was sealed by heat, and after heat treatment in an oil bath, the number of spoiled tubes after storage at 55 ° C. for 3 weeks was examined. Circulating temperature in filler valve (filling temperature), the presence or absence of milk components attached at the filler valves, the dissolution existence of mass in time varying over the tube number and heat treatment shown in Table 19.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 蔗糖脂肪酸エステルを含まないミルク入
り低酸性飲料内容液を調合し、均質化処理を行う前また
は行った後熱交換機による加熱処理を行い、次いで内容
液を容器に充填密閉した後レトルト加熱処理を行い、熱
交換機による加熱処理とレトルト加熱処理のF0 値の合
計を120以上とすることを特徴とする密閉容器入り低
酸性飲料の製造方法。
1. A low-acid beverage content liquid containing milk that does not contain sucrose fatty acid ester is prepared and heat-treated by a heat exchanger before or after homogenization treatment, and then after filling the container with the content liquid and sealing. A method for producing a low-acid beverage in a closed container, which comprises performing retort heat treatment and setting a total of F 0 values of heat treatment by a heat exchanger and retort heat treatment to 120 or more.
【請求項2】 熱交換機による加熱処理のF0 値をレト
ルト加熱処理のF0値よりも大きくすることを特徴とす
る請求項1記載の製造方法。
2. A process according to claim 1, wherein the the F 0 value of heat treatment by a heat exchanger larger than the F 0 value of retort heat treatment.
【請求項3】 前記熱交換機による加熱処理を2段以上
に分けて行うことを特徴とする請求項1または2記載の
製造方法。
3. The manufacturing method according to claim 1, wherein the heat treatment by the heat exchanger is performed in two or more stages.
【請求項4】 フィラーにより内容液を容器に充填し、
その際の充填温度を35℃以下とすることを特徴とする
請求項1〜3のいずれかに記載の製造方法。
4. A container is filled with the content liquid with a filler,
The manufacturing method according to any one of claims 1 to 3, wherein the filling temperature at that time is set to 35 ° C or lower.
【請求項5】 該容器に内容液を充填した後容器を密閉
する前に容器内の空気を、水蒸気または窒素ガスと水蒸
気の混合ガスにより置換することを特徴とする請求項4
記載の製造方法。
5. The air in the container is replaced by steam or a mixed gas of nitrogen gas and steam after the container is filled with the content liquid and before the container is closed.
The manufacturing method described.
JP6250077A 1994-09-19 1994-09-19 Production of low-acidic beverage filled in hermetically sealed container Pending JPH0884576A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6250077A JPH0884576A (en) 1994-09-19 1994-09-19 Production of low-acidic beverage filled in hermetically sealed container

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6250077A JPH0884576A (en) 1994-09-19 1994-09-19 Production of low-acidic beverage filled in hermetically sealed container

Publications (1)

Publication Number Publication Date
JPH0884576A true JPH0884576A (en) 1996-04-02

Family

ID=17202473

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6250077A Pending JPH0884576A (en) 1994-09-19 1994-09-19 Production of low-acidic beverage filled in hermetically sealed container

Country Status (1)

Country Link
JP (1) JPH0884576A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0865735A1 (en) * 1997-03-19 1998-09-23 Societe Des Produits Nestle S.A. Process for sterilising beverages
JP2000228952A (en) * 1999-02-10 2000-08-22 Asahi Soft Drinks Co Ltd Method for preventing generation of off-flavor of nonalcoholic palatable beverage with milk and the palatable beverage filled in transparent vessel
EP1133244A4 (en) * 1998-11-25 2002-04-17 William F Aftoora Liquefied water soluble acidity-reducing formulation for food and beverage products

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0865735A1 (en) * 1997-03-19 1998-09-23 Societe Des Produits Nestle S.A. Process for sterilising beverages
EP1133244A4 (en) * 1998-11-25 2002-04-17 William F Aftoora Liquefied water soluble acidity-reducing formulation for food and beverage products
JP2000228952A (en) * 1999-02-10 2000-08-22 Asahi Soft Drinks Co Ltd Method for preventing generation of off-flavor of nonalcoholic palatable beverage with milk and the palatable beverage filled in transparent vessel

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