JP2011103785A - Container-packed, low-acid beverage and method for producing the same - Google Patents
Container-packed, low-acid beverage and method for producing the same Download PDFInfo
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- JP2011103785A JP2011103785A JP2009259950A JP2009259950A JP2011103785A JP 2011103785 A JP2011103785 A JP 2011103785A JP 2009259950 A JP2009259950 A JP 2009259950A JP 2009259950 A JP2009259950 A JP 2009259950A JP 2011103785 A JP2011103785 A JP 2011103785A
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- 235000013361 beverage Nutrition 0.000 title claims abstract description 113
- 239000002253 acid Substances 0.000 title claims abstract description 88
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 32
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 claims abstract description 190
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 186
- 235000017557 sodium bicarbonate Nutrition 0.000 claims abstract description 95
- 229910000030 sodium bicarbonate Inorganic materials 0.000 claims abstract description 95
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 93
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 92
- 238000007789 sealing Methods 0.000 claims abstract description 23
- 239000000203 mixture Substances 0.000 claims abstract description 4
- 239000007789 gas Substances 0.000 claims description 61
- 235000013353 coffee beverage Nutrition 0.000 claims description 48
- 239000004033 plastic Substances 0.000 claims description 23
- 229920003023 plastic Polymers 0.000 claims description 23
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 19
- 238000011049 filling Methods 0.000 claims description 19
- 235000013616 tea Nutrition 0.000 claims description 15
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 claims description 12
- 229910052751 metal Inorganic materials 0.000 claims description 11
- 239000002184 metal Substances 0.000 claims description 11
- 229910001873 dinitrogen Inorganic materials 0.000 claims description 8
- 238000010790 dilution Methods 0.000 claims description 7
- 239000012895 dilution Substances 0.000 claims description 7
- UIIMBOGNXHQVGW-DEQYMQKBSA-M Sodium bicarbonate-14C Chemical compound [Na+].O[14C]([O-])=O UIIMBOGNXHQVGW-DEQYMQKBSA-M 0.000 claims description 5
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical class [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 5
- 238000009472 formulation Methods 0.000 claims 1
- 238000003756 stirring Methods 0.000 abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 12
- 238000007865 diluting Methods 0.000 abstract description 4
- 238000003860 storage Methods 0.000 abstract description 4
- 230000002950 deficient Effects 0.000 abstract description 2
- 150000003839 salts Chemical class 0.000 abstract 1
- 229920006395 saturated elastomer Polymers 0.000 abstract 1
- 235000016213 coffee Nutrition 0.000 description 31
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 23
- 239000000243 solution Substances 0.000 description 22
- 239000007788 liquid Substances 0.000 description 20
- 239000008267 milk Substances 0.000 description 16
- 210000004080 milk Anatomy 0.000 description 16
- 235000013336 milk Nutrition 0.000 description 15
- 230000000694 effects Effects 0.000 description 10
- 238000002360 preparation method Methods 0.000 description 10
- 239000000796 flavoring agent Substances 0.000 description 8
- 235000019634 flavors Nutrition 0.000 description 8
- 238000005187 foaming Methods 0.000 description 8
- 238000002156 mixing Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 238000010979 pH adjustment Methods 0.000 description 7
- 238000010438 heat treatment Methods 0.000 description 6
- 150000002500 ions Chemical class 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- 238000004080 punching Methods 0.000 description 6
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 5
- 230000007423 decrease Effects 0.000 description 5
- 238000011156 evaluation Methods 0.000 description 5
- 239000006260 foam Substances 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 229920000139 polyethylene terephthalate Polymers 0.000 description 5
- 239000005020 polyethylene terephthalate Substances 0.000 description 5
- -1 polypropylene Polymers 0.000 description 5
- 239000004743 Polypropylene Substances 0.000 description 4
- 239000012790 adhesive layer Substances 0.000 description 4
- 230000005587 bubbling Effects 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 229920001155 polypropylene Polymers 0.000 description 4
- 241001122767 Theaceae Species 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 238000004090 dissolution Methods 0.000 description 3
- 238000002474 experimental method Methods 0.000 description 3
- 239000012467 final product Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 239000012488 sample solution Substances 0.000 description 3
- 239000003566 sealing material Substances 0.000 description 3
- 230000001954 sterilising effect Effects 0.000 description 3
- 238000004659 sterilization and disinfection Methods 0.000 description 3
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 238000012790 confirmation Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 238000004817 gas chromatography Methods 0.000 description 2
- 238000001879 gelation Methods 0.000 description 2
- 235000021552 granulated sugar Nutrition 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 235000020185 raw untreated milk Nutrition 0.000 description 2
- 239000000523 sample Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 235000019640 taste Nutrition 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 229920000219 Ethylene vinyl alcohol Polymers 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000003957 anion exchange resin Substances 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 235000006708 antioxidants Nutrition 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 229960005070 ascorbic acid Drugs 0.000 description 1
- 235000010323 ascorbic acid Nutrition 0.000 description 1
- 239000011668 ascorbic acid Substances 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 235000020152 coffee milk drink Nutrition 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000012937 correction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000008034 disappearance Effects 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 239000005457 ice water Substances 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 239000003002 pH adjusting agent Substances 0.000 description 1
- 238000009527 percussion Methods 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 235000019643 salty taste Nutrition 0.000 description 1
- 235000020183 skimmed milk Nutrition 0.000 description 1
- 230000004936 stimulating effect Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 235000000346 sugar Nutrition 0.000 description 1
- 230000036962 time dependent Effects 0.000 description 1
- 235000008939 whole milk Nutrition 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
- A23L2/52—Adding ingredients
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
- A23F3/00—Tea; Tea substitutes; Preparations thereof
- A23F3/16—Tea extraction; Tea extracts; Treating tea extract; Making instant tea
- A23F3/163—Liquid or semi-liquid tea extract preparations, e.g. gels, liquid extracts in solid capsules
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
- A23F5/00—Coffee; Coffee substitutes; Preparations thereof
- A23F5/24—Extraction of coffee; Coffee extracts; Making instant coffee
- A23F5/243—Liquid, semi-liquid or non-dried semi-solid coffee extract preparations; Coffee gels; Liquid coffee in solid capsules
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Dispersion Chemistry (AREA)
- Tea And Coffee (AREA)
- Non-Alcoholic Beverages (AREA)
Abstract
Description
本発明は、プラスチックボトル、プラスチックカップ、金属缶等の容器に充填密封して販売されるコーヒー飲料、茶飲料等の低酸性飲料及び其の製造方法に関し、特に、ホットウォーマーで加温販売されても容器変形や密封不良が生じない容器詰め低酸性飲料およびその製造方法に関する。 The present invention relates to low acid beverages such as coffee beverages and tea beverages that are sold by being filled and sealed in containers such as plastic bottles, plastic cups, and metal cans, and a method for producing the same. The present invention also relates to a container-packed low-acid beverage that does not cause container deformation or poor sealing and a method for producing the same.
コーヒー飲料や茶飲料等の低酸性飲料は、調合時には一般に高濃度の抽出液が用いられている。高濃度抽出液(エキス)はコーヒーエキスのようにそれ自体のpHが低い場合や、茶飲料のエキスのように酸化防止剤として添加されるアスコルビン酸によりpHが低くなっている場合がある。そして、最終製品のpHが低いと酸味が強くなるため、最終製品とする調合のいずれかの段階でpHを調整する必要がある。また、乳成分を混合したミルクコーヒー飲料やミルクティーなどでは、調合時のpHが低いあるいは高過ぎると乳成分等の飲料内容物が凝固沈殿する、あるいはゲル状となる傾向がある。従って、従来はコーヒー飲料、茶飲料等の低酸性飲料を製造するにあたり、pHを調整して飲料内容物の調合を行なっており、pH調整剤としては、調整が容易であり、内容物の劣化に伴うpH低下を抑制できることから、緩衝効果を有する重曹(炭酸水素ナトリウム)が多用されてきた。 In the case of a low acid beverage such as a coffee beverage or a tea beverage, a high concentration extract is generally used at the time of preparation. The high-concentration extract (extract) may have a low pH due to its own pH, such as a coffee extract, or may be lowered by ascorbic acid added as an antioxidant, such as an extract of a tea beverage. And since the sourness becomes strong when the pH of the final product is low, it is necessary to adjust the pH at any stage of the preparation of the final product. In addition, in milk coffee drinks and milk tea mixed with milk components, when the pH at the time of preparation is low or too high, the beverage contents such as milk components tend to coagulate and precipitate or become gel. Therefore, conventionally, when producing low acid beverages such as coffee beverages and tea beverages, the pH is adjusted to prepare the beverage content. As a pH adjuster, the adjustment is easy and the content deteriorates. Since it is possible to suppress a decrease in pH associated with sodium bicarbonate, sodium bicarbonate (sodium bicarbonate) having a buffering effect has been frequently used.
そして、最近PETボトル詰め飲料やカップ詰飲料が加温販売されるようになり、容器詰め低酸性飲料もホットウォーマーでの加温販売が多くなってきたが、この場合ホットウォーマーでの保存中にPETボトルやカップが変形したり、密封不良を起こすことが問題となっている。本発明者らは、検討の結果、このような容器変形や密封不良は、調合時に添加された重曹由来の炭酸ガス(二酸化炭素)、および容器のヘッドスペースの空気を置換するため充填シール時に用いられる窒素・炭酸ガス混合ガスからなる置換ガス由来の炭酸ガスによる膨張が影響していることを突き止めた。すなわち、重曹由来の炭酸ガスおよびヘッドスペース置換のための混合ガス由来の炭酸ガスは、常温下ではそのほとんどが飲料内容物中にガスまたはイオンの状態で溶解しているが、ホットウォーマーで60℃以上、例えば75℃程度に加熱されると、ヘッドスペースの膨張の他に飲料より炭酸ガスと水蒸気が発生し、ヘッドスペース中に出てきて容器を膨張させる。その際、ヘッドスペース置換での混合ガス由来の炭酸ガスの膨張分以上に重曹由来の炭酸ガスの膨張分が大きいために容器変形や密封不良を生じるのである。なお、内容物である飲料の温度はホットウォーマーでの速熱モード時などには75℃、更にはそれ以上になることがある。 And recently, PET bottled beverages and cupped beverages have been warmed and sold, and container-packed low-acid beverages have also been warmed and sold in hot warmers. In this case, while being stored in hot warmers, The problem is that PET bottles and cups are deformed and cause poor sealing. As a result of the study, the present inventors have studied that such container deformation and poor sealing are used at the time of filling and sealing in order to replace carbon dioxide (carbon dioxide) derived from baking soda added during preparation and air in the headspace of the container. It was found that the expansion by carbon dioxide gas derived from the substitution gas consisting of a mixed gas of nitrogen and carbon dioxide is influential. That is, the carbon dioxide gas derived from baking soda and the carbon dioxide gas derived from the mixed gas for head space replacement are mostly dissolved in the beverage content in the form of gas or ions at room temperature, but at 60 ° C. with a hot warmer. As described above, for example, when heated to about 75 ° C., carbon dioxide gas and water vapor are generated from the beverage in addition to the expansion of the head space, and come out into the head space to expand the container. At this time, since the expansion of the carbon dioxide gas derived from the baking soda is larger than the expansion of the carbon dioxide gas derived from the mixed gas in the head space replacement, the container is deformed and the sealing is poor. It should be noted that the temperature of the beverage as the contents may be 75 ° C. or higher when in the rapid heating mode with a hot warmer.
一方缶入りコーヒー飲料等金属缶詰め低酸性飲料の製造工程において、不良缶を打検により検出する場合にも、同様に重曹由来の炭酸ガスの発生により缶内圧が変化し、残存する炭酸ガス量が多い場合にレトルト殺菌時の容器変形の発生、あるいは打検精度が低下する問題も生じている。 On the other hand, in the manufacturing process of metal canned low acid beverages such as canned coffee beverages, even when defective cans are detected by punching, the internal pressure of the can changes due to the generation of carbon dioxide derived from baking soda, and the amount of carbon dioxide remaining In many cases, there is a problem that the container is deformed at the time of retort sterilization or the accuracy of punching is lowered.
特許文献1は、コーヒー飲料や紅茶飲料のpH調節時における重曹の添加に基づく塩味を低減し、製品の香味を改善するために、陰イオン交換樹脂を通して得られるpHが8.0以上のアルカリイオン水を用いてコーヒーまたは茶の抽出を行うことにより重曹の添加量を低減させる方法を開示している。 Patent Document 1 describes alkali ions having a pH of 8.0 or more obtained through an anion exchange resin in order to reduce the salty taste based on the addition of baking soda during the pH adjustment of coffee beverages and tea beverages and to improve the flavor of the product. A method of reducing the amount of sodium bicarbonate added by extracting coffee or tea with water is disclosed.
しかしながら、この方法によれば、アルカリイオン水を得るために特別な設備が必要であり、既設の容器詰め低酸性飲料製造装置にそのまま適用することはできないので、設備の新設のために大きなコストを必要とする。 However, according to this method, special equipment is required to obtain alkaline ionized water, and it cannot be applied as it is to an existing container-packed low-acid beverage production apparatus. I need.
また、特許文献2は、乳成分を含有するコーヒー飲料や茶飲料において重曹添加による風味、品質の劣化を惹き起こすことなく凝集、沈殿、混濁等を防止するために、乳成分未添加液、乳成分含有液、乳成分混合液のいずれかひとつの調整工程において、窒素のバブリングによって溶存気体を除去することを開示している。 Patent Document 2 discloses a milk component-free solution, milk, and the like in order to prevent agglomeration, precipitation, turbidity and the like without causing flavor and quality deterioration due to addition of baking soda in coffee beverages and tea beverages containing milk components. It discloses that dissolved gas is removed by bubbling nitrogen in any one adjustment step of the component-containing liquid and the milk component mixed solution.
しかしながら、この方法によれば、窒素バブリングによって重曹の添加量を低減することにより風味の劣化を防止することはできても、窒素バブリングを行うこと自体によって飲料の風味を損なうという新たな問題を生じる。 However, according to this method, although the deterioration of flavor can be prevented by reducing the amount of sodium bicarbonate added by nitrogen bubbling, a new problem arises in that the flavor of the beverage is impaired by nitrogen bubbling itself. .
本発明は、上記従来の容器詰め低酸性飲料の製造方法における問題点にかんがみなされたものであって、本発明の目的は、容器詰め低酸性飲料の調合時に味覚の点で適正なpHを達成するとともに、乳成分等の添加による飲料内容物の凝固沈殿、あるいはゲル化を防止しながら、pH調節のために添加される重曹由来の炭酸ガスおよび容器のヘッドスペースの空気を置換するための窒素・炭酸ガス混合ガス由来の炭酸ガスによりホットウォーマー保存中に生じる容器変形や密封不良ならびに製造工程における打検精度の低下の問題を既設の製造設備に大幅な変更を加えることなく、また窒素バブリングにより飲料の風味、香味を損なうことなく簡単に解決できる容器詰め低酸性飲料およびその製造方法を提供することにある。 The present invention has been considered in view of the above problems in the conventional method for producing a packaged low-acid beverage, and the object of the present invention is to achieve an appropriate pH in terms of taste when preparing a packaged low-acid beverage. At the same time, while preventing the coagulation precipitation or gelation of the beverage contents due to the addition of milk components, etc., carbon dioxide derived from baking soda added for pH adjustment and nitrogen for replacing the air in the container headspace・ Contains problems such as container deformation and poor sealing caused by carbon dioxide gas derived from carbon dioxide mixed gas during storage of hot warmers, as well as a decrease in accuracy of inspection in the manufacturing process, without significant changes to existing manufacturing equipment, and by nitrogen bubbling. An object of the present invention is to provide a container-packed low-acid beverage that can be easily solved without impairing the flavor and flavor of the beverage and a method for producing the same.
本発明者らは、上記目的を達成するために種々実験と研究を重ねた結果、低酸性飲料の味覚の点で適正なpHを達成するとともに、調合時に乳成分等の添加による飲料内容物の凝固沈殿、あるいはゲル化を防止するために必要なpH調節のために重曹は添加するが、飲料の調合時に、高濃度、高温状態にある低酸性飲料に重曹を添加、撹拌して前記重曹より炭酸ガスを発泡させて除去した後、飲料を希釈して乳成分等の調合工程を行い、この調合工程を終了した飲料を容器に充填密封すれば、ホットウォーマーにおける保存中に重曹由来の炭酸ガスの発生、膨張を顕著に抑制することができ、ヘッドスペース置換ガス由来の炭酸ガスの膨張があっても容器変形や密封不良を充分に防止することができ、また製造工程において打検精度を低下させることもないことを見出し、本発明に到達した。 As a result of repeating various experiments and researches to achieve the above object, the present inventors have achieved an appropriate pH in terms of the taste of a low acid beverage, and at the same time, the content of the beverage by adding milk components etc. Baking soda is added to adjust the pH necessary to prevent coagulation precipitation or gelation. At the time of beverage preparation, baking soda is added to a highly acidic, low-acid beverage in a high temperature state, stirred and mixed with the sodium bicarbonate. After removing the carbon dioxide gas by foaming, if the beverage is diluted to prepare the milk component, etc., the beverage after completion of this preparation step is filled and sealed in a container, and the carbon dioxide gas derived from sodium bicarbonate during storage in the hot warmer Generation and expansion can be remarkably suppressed, and even if there is expansion of carbon dioxide gas derived from the headspace replacement gas, container deformation and sealing failure can be sufficiently prevented, and the accuracy of punching is reduced in the manufacturing process. The It found that no Rukoto, have reached the present invention.
すなわち、上記目的を達成する本発明の第1の構成は、重曹によりpH調整された容器詰め低酸性飲料において、pH4以下の飽和食塩水中で捕集した際のヘッドスペースの単位容積当たりの炭酸ガス濃度が、25℃保管時で10%以下、且つ75℃保管時で20%以下であることを特徴とする容器詰め低酸性飲料である。 That is, the first configuration of the present invention that achieves the above object is a carbon dioxide gas per unit volume of the headspace when collected in a saturated saline solution having a pH of 4 or less in a container-filled low-acid beverage adjusted in pH with sodium bicarbonate. A container-packed low-acid beverage characterized by a concentration of 10% or less when stored at 25 ° C. and 20% or less when stored at 75 ° C.
本発明の第2の構成は、第1の構成に加え、重曹の添加量から求められる総炭酸量に対し、充填密封後の容器内の総炭酸量が45%以下である容器詰め低酸性飲料である。 In addition to the first configuration, the second configuration of the present invention is a container-packed low-acid beverage in which the total carbonic acid content in the container after filling and sealing is 45% or less with respect to the total carbonic acid amount obtained from the added amount of baking soda It is.
本発明の第3の構成は、第1または第2の構成に加え、充填時にヘッドスペースを窒素ガスと炭酸ガスの混合ガスでガス置換した容器詰め低酸性飲料である。 A third configuration of the present invention is a container-packed low-acid beverage in which the head space is replaced with a mixed gas of nitrogen gas and carbon dioxide during filling in addition to the first or second configuration.
本発明の第4の構成は、第1〜第3のいずれかの構成に加え、低酸性飲料がコーヒー飲料または茶飲料である容器詰め低酸性飲料である。 The fourth configuration of the present invention is a container-packed low acid beverage in which the low acid beverage is a coffee beverage or a tea beverage in addition to any of the first to third configurations.
本発明の第5の構成は、第1〜第4のいずれかの構成に加え、容器がプラスチックボトル、プラスチックカップまたは金属缶である容器詰め低酸性飲料である。 A fifth configuration of the present invention is a container-packed low-acid beverage in which the container is a plastic bottle, a plastic cup, or a metal can in addition to any of the first to fourth configurations.
本発明の第6の構成は、重曹によりpH調整された容器詰め低酸性飲料の製造方法において、高濃度、高温状態の低酸性飲料に重曹を添加、撹拌して前記重曹より炭酸ガスを除去した後、飲料を希釈して調合を行い、容器に充填密封することを特徴とする容器詰め低酸性飲料の製造方法である。 According to a sixth aspect of the present invention, in the method for producing a container-packed low-acid beverage whose pH is adjusted with sodium bicarbonate, sodium bicarbonate is added to and stirred in a high-concentration, high-temperature, low-acid beverage to remove carbon dioxide from the sodium bicarbonate. Then, it is a manufacturing method of the container-packed low-acid drink characterized by diluting and preparing a drink and filling and sealing a container.
本発明の第7の構成は、第6の構成に加え、前記低酸性飲料の濃度が希釈後の濃度の2倍以上で、pHが6以下である容器詰め低酸性飲料の製造方法である。 The 7th structure of this invention is a manufacturing method of the container-packed low-acid drink in which the density | concentration of the said low-acid drink is 2 times or more of the density | concentration after dilution, and pH is 6 or less in addition to a 6th structure.
本発明の第8の構成は、第6または第7の構成に加え、前記低酸性飲料の温度が50℃以上である容器詰め低酸性飲料の製造方法である。 The 8th structure of this invention is a manufacturing method of the container stuffing low acid drink whose temperature of the said low acid drink is 50 degreeC or more in addition to the 6th or 7th structure.
本発明の第9の構成は、第6〜第8のいずれかの構成に加え、重曹の添加量から求められる総炭酸量に対し、充填密封後の重曹由来の炭酸量が45%以下とする容器詰め低酸性飲料の製造方法である。 In the ninth configuration of the present invention, in addition to any of the sixth to eighth configurations, the amount of carbonate derived from baking soda after filling and sealing is 45% or less with respect to the total amount of carbonate determined from the amount of sodium bicarbonate added. It is a manufacturing method of a container-packed low-acid drink.
本発明の第10の構成は、第6〜第9のいずれかの構成に加え、充填時にヘッドスペースを窒素ガスと炭酸ガスの混合ガスでガス置換する容器詰め低酸性飲料の製造方法である。 A tenth configuration of the present invention is a method for producing a container-filled low-acid beverage in which the headspace is replaced with a mixed gas of nitrogen gas and carbon dioxide gas at the time of filling, in addition to any of the sixth to ninth configurations.
本発明の第11の構成は、第6〜第10の構成に加え、低酸性飲料がコーヒー飲料または茶飲料である容器詰め低酸性飲料の製造方法である。 The 11th structure of this invention is a manufacturing method of the container stuffing low acid drink whose low acid drink is a coffee drink or a tea drink in addition to the 6th-10th structure.
本発明の第12の構成は、第6〜第11のいずれかの構成に加え、容器がプラスチックボトル、プラスチックカップまたは金属缶である容器詰め低酸性飲料の製造方法である。 The twelfth configuration of the present invention is a method for producing a container-filled low-acid beverage in which the container is a plastic bottle, a plastic cup or a metal can in addition to any of the sixth to eleventh configurations.
本発明の容器詰め低酸性飲料によれば、飲料の調合時に重曹由来の炭酸ガス量を著しく低減してあるので、ヘッドスペース中に窒素ガスと炭酸ガスの混合ガスで置換することによる混合ガス由来の炭酸ガスが存在していても、飲料中に含まれる総炭酸ガス量は顕著に低減しており、容器を加温販売のためにホットウォーマーにより長期間保存しても、炭酸ガスの発生および膨張による容器変形や密封不良が生じることがなく、また容器が金属缶の場合は缶の膨張による製造工程中の打検精度の低下も防止することでき、打検精度の高い製品を提供することができる。 According to the container-packed low-acid beverage of the present invention, the amount of carbon dioxide derived from baking soda is remarkably reduced during the preparation of the beverage, so the mixed gas is derived by substituting a mixed gas of nitrogen gas and carbon dioxide in the headspace. Even if the amount of carbon dioxide is present, the total amount of carbon dioxide contained in the beverage is remarkably reduced. Even if the container is stored for a long period of time with a hot warmer for warm sales, the generation of carbon dioxide and Providing a product with high punching accuracy that does not cause container deformation or sealing failure due to expansion, and can prevent a decrease in punching accuracy during the manufacturing process due to expansion of the can when the container is a metal can. Can do.
また、本発明の容器詰め低酸性飲料の製造方法によれば、高濃度、高温状態にある低酸性飲料に重曹を添加、攪拌して重曹から炭酸ガスを除去した後飲料を希釈して調合を行い、容器に充填密封することにより、調合時に特別の装置を使用することなく、既設の低酸性飲料製造設備を利用して簡単に重曹由来の炭酸ガスを除去してヘッドスペース中の単位容積あたりの炭酸ガス濃度を大幅に減少させることができる。 In addition, according to the method for producing a containerized low-acid beverage of the present invention, sodium bicarbonate is added to a low-acid beverage in a high concentration, high-temperature state, and the beverage is diluted by diluting the beverage after removing carbon dioxide from the sodium bicarbonate. Per unit volume in the headspace by simply removing the carbon dioxide derived from baking soda using existing low-acid beverage production equipment without using special equipment during compounding. The carbon dioxide concentration of can be greatly reduced.
本発明は、PETボトル等のプラスチックボトルやポリプロピレンカップ等のプラスチックカップ等重曹を添加した内容物を充填密封してホットウォーマーで加温販売する際に重曹由来の炭酸ガスにより容器変形や密封不良を生じやすい容器に適用することができる。また、本発明は、重曹を添加した内容物を充填密封した金属缶の打検精度を向上させるために金属缶にも適用することができる。 In the present invention, when a plastic bottle such as a PET bottle or a plastic cup such as a polypropylene cup is filled and sealed with a baking soda and heated with a hot warmer, the container is deformed or poorly sealed due to carbon dioxide derived from the baking soda. It can be applied to containers that are prone to occur. The present invention can also be applied to metal cans in order to improve the accuracy of punching of metal cans that are filled and sealed with contents to which sodium bicarbonate is added.
本発明が適用される飲料は、pH調整のために重曹の添加が必要な低酸性飲料であり、コーヒー飲料および茶飲料がその代表的なものであるが、これに限定されるものではない。 Beverages to which the present invention is applied are low-acid beverages that require the addition of baking soda for pH adjustment, and coffee beverages and tea beverages are typical, but are not limited thereto.
実験の結果、重曹によりpH調整された容器詰め低酸性飲料において、pH4以下の飽和食塩水中で捕集した際のヘッドスペースの単位容積当たりの炭酸ガス濃度が、25℃保管時で10%以下であり、かつ75℃保管時で20%以下であるときは、ヘッドスペースの炭酸ガスの膨張によりプラスチック容器が変形したり密封不良を生じることがなく、したがってホットウォーマーで加温販売してもこのような不具合が生じるおそれがなく、また容器が金属缶の場合にはヘッドスペースの炭酸ガスの膨張による打検精度の低下を生じるおそれがないことが判った。 As a result of the experiment, the concentration of carbon dioxide gas per unit volume of the head space when collected in a saturated saline solution having a pH of 4 or less was 10% or less when stored at 25 ° C. If it is 20% or less when stored at 75 ° C., the expansion of the carbon dioxide gas in the head space will not cause the plastic container to be deformed or cause a sealing failure. It has been found that there is no possibility of causing a problem, and in the case where the container is a metal can, there is no possibility of causing a decrease in percussion accuracy due to the expansion of carbon dioxide in the head space.
ヘッドスペースの単位容積あたりの炭酸ガス濃度を上記範囲内に抑えるには、重曹の添加量から求められる総炭酸量に対し、充填密封後の容器内の総炭酸量を45%以下にする必要がある。充填密封後の容器内の総炭酸量(重曹由来およびヘッドスペースの置換ガス由来の炭酸量)は飲料中に溶解している分とヘッドスペース中に存在している量から、次の方法により確認することができる。 In order to keep the carbon dioxide concentration per unit volume of the head space within the above range, the total amount of carbon dioxide in the container after filling and sealing must be 45% or less with respect to the total amount of carbon dioxide obtained from the amount of sodium bicarbonate added. is there. The total amount of carbonic acid in the container after filling and sealing (carbonic acid derived from baking soda and headspace replacement gas) is confirmed by the following method from the amount dissolved in the beverage and the amount present in the headspace. can do.
飲料中において溶存炭酸ガスは単一分子(CO2)の状態と炭酸水素イオン(HCO3 −)、炭酸イオン(CO3 2−)の状態で存在し、定常状態ではそれぞれが電離平衡状態にあると考えられる。また、それぞれの存在率は飲料のpHによって異なると考えられ、pHが4以下ではほとんどが単一分子(CO2)の状態で存在し、pHが高くなるに従い炭酸水素イオン(HCO3 −)が増え、pHが8を越えると単一分子(CO2)はほとんど存在しなくなり、炭酸水素イオン(HCO3 −)の他に炭酸イオン(CO3 2−)が存在しはじめる。飲料中の総炭酸濃度と単一分子(CO2)の濃度は、後述する実験例のように、東興化学研究所製の炭酸ガス濃度測定器(Ti−9004)やTCD(熱伝導度)センサー方式を用いたハックウルトラ社製の溶存炭酸ガス濃度計(モデル3658)などを用いることができる。総炭酸濃度(Call)は飲料のpHを4以下にして測定できる。pH調整を行わないで測定した値を単一分子(CO2)すなわち炭酸ガス状態での溶解濃度(Cgas)として評価できる。これらにより、イオンとして溶解している濃度(Cion)は
Cion=Call−Cgas
として、炭酸水素イオン(HCO3 −)濃度と炭酸イオン(CO3 2−)濃度の合計量として求められる。これらの値と飲料の充填量から、飲料中の総炭酸量、炭酸ガス(CO2)量、イオン量を求めることができる。
Dissolved carbon dioxide in beverages exists in a single molecule (CO 2 ) state, a bicarbonate ion (HCO 3 − ), and a carbonate ion (CO 3 2− ) state, and each is in an ionization equilibrium state in a steady state. it is conceivable that. Each abundance is considered to vary depending on the pH of the beverage. When the pH is 4 or less, most of them exist in a single molecule (CO 2 ) state, and as the pH increases, bicarbonate ions (HCO 3 − ) are present. When the pH increases and exceeds 8, single molecules (CO 2 ) hardly exist, and carbonate ions (CO 3 2− ) begin to exist in addition to hydrogen carbonate ions (HCO 3 − ). The total carbonic acid concentration and single molecule (CO 2 ) concentration in beverages are measured by carbon dioxide concentration meter (Ti-9004) and TCD (thermal conductivity) sensor manufactured by Toko Chemical Laboratories as in the experimental examples described later. A dissolved carbon dioxide concentration meter (model 3658) manufactured by Hack Ultra Co., Ltd. using the method can be used. The total carbonic acid concentration (Call) can be measured by setting the pH of the beverage to 4 or less. A value measured without adjusting the pH can be evaluated as a single molecule (CO 2 ), that is, a dissolved concentration (Cgas) in a carbon dioxide state. As a result, the concentration dissolved as ions (Cion) is Cion = Call-Cgas.
As the total amount of the bicarbonate ion (HCO 3 − ) concentration and the carbonate ion (CO 3 2− ) concentration. From these values and the filling amount of the beverage, the total amount of carbonic acid, the amount of carbon dioxide (CO 2 ), and the amount of ions in the beverage can be determined.
次に、ヘッドスペース中の炭酸ガス量(Vco2)は、常温下においてヘッドスペースガスをpH4以下の飽和食塩水中で捕集し、捕集ガスをガスクロマトグラフィーや既知の炭酸ガス濃度測定器を用いて測定される炭酸ガス濃度(Hco2)と、捕集したガス量(Vall)との積
Vco2=Vall×Hco2
から求めることができる。
Next, the amount of carbon dioxide gas in the headspace (Vco2) is obtained by collecting the headspace gas in a saturated saline solution having a pH of 4 or less at room temperature, and using gas chromatography or a known carbon dioxide concentration measuring device for the collected gas. Product of carbon dioxide concentration (Hco2) measured and the amount of collected gas (Vall) Vco2 = Vall × Hco2
Can be obtained from
充填密封後の容器内の総炭酸量(重曹由来およびヘッドスペースの置換ガス由来の炭酸量)はCallとVco2の合計値として求められる。理論上の重曹(炭酸水素ナトリウムNaHCO3)に含まれる炭酸ガス量は重曹の添加量の52.4重量%であることから、一容器当たりの重曹の添加量の52.4重量%と一容器内の総炭酸量とから、重曹由来の炭酸量に対する残存率が評価できる。 The total amount of carbonic acid (the amount of carbonic acid derived from baking soda and the head space replacement gas) in the container after filling and sealing is obtained as the sum of Call and Vco2. The amount of carbon dioxide contained in the theoretical baking soda (sodium bicarbonate NaHCO 3 ) is 52.4% by weight of the added amount of baking soda, so 52.4% by weight of the added amount of baking soda per container and one container The residual rate with respect to the amount of carbonic acid derived from baking soda can be evaluated from the total amount of carbonic acid.
なお、ヘッドスペースの炭酸ガスと飲料中の溶存炭酸ガス(単一分子(CO2))は溶解平衡状態にあり、更に溶存炭酸ガス(単一分子(CO2))と炭酸水素イオン(HCO3 −)、炭酸イオン(CO3 2−)とはそれぞれが電離平衡状態にある。また、コーヒー飲料や茶飲料のpHが6から7程度の範囲にあることから、重曹の添加量から求められる総炭酸量に対し、充填密封後の総炭酸量を45%以下にできるのであれば、ホットウォーマーでの膨張を減らすことができ、容器変形や密封不良を防止することができる。更に、ヘッドスペースの炭酸ガスと溶存炭酸ガスとは溶解平衡にあることから、ヘッドスペース内の25℃保管時で10%以下、且つ75℃保管時で20%以下である時は、容器変形や密封不良を防止できる。 The carbon dioxide gas in the head space and the dissolved carbon dioxide gas (single molecule (CO 2 )) in the beverage are in a solution equilibrium state, and further the dissolved carbon dioxide gas (single molecule (CO 2 )) and hydrogen carbonate ion (HCO 3). - ) And carbonate ions (CO 3 2− ) are in an ionization equilibrium state. Moreover, since the pH of coffee beverages and tea beverages is in the range of about 6 to 7, if the total amount of carbonate after filling and sealing can be reduced to 45% or less with respect to the total amount of carbonate determined from the amount of sodium bicarbonate added. The expansion in the hot warmer can be reduced, and the container deformation and the sealing failure can be prevented. Furthermore, since the carbon dioxide and dissolved carbon dioxide in the head space are in a dissolution equilibrium, when the head space is stored at 25 ° C. at 10% or less and at 75 ° C. is stored at 20% or less, container deformation or Sealing failure can be prevented.
また、ヘッドスペースの単位容積あたりの炭酸ガス濃度を上記範囲内に抑えることができれば、低酸性飲料の容器への充填時に容器のヘッドスペースの空気を窒素ガスと炭酸ガスの混合ガスでガス置換しても差し支えない。 If the carbon dioxide concentration per unit volume of the head space can be kept within the above range, the air in the head space of the container is replaced with a mixed gas of nitrogen gas and carbon dioxide when filling the container of the low acid beverage. There is no problem.
次に、上記重曹によりpH調整された容器詰め低酸性飲料の製造方法について述べる。
本発明に係る容器詰め低酸性飲料の製造方法の特徴は、重曹によりpH調整された容器詰め低酸性飲料の製造方法において、高濃度、高温状態の低酸性飲料に重曹を添加、撹拌して前記重曹より炭酸ガスを除去した後、飲料を希釈して調合を行い、容器に充填密封することにある。
Next, a method for producing a container-packed low-acid beverage whose pH has been adjusted with the baking soda will be described.
The characteristics of the method for producing a container-packed low-acid beverage according to the present invention are as follows. After removing carbon dioxide from baking soda, the beverage is diluted and mixed, and the container is filled and sealed.
重曹を添加する前のコーヒー飲料、茶飲料等の低酸性飲料のpHは通常6以下である。そして本発明の目的を達成する低酸性飲料を効率的に製造するには、重曹を添加する前の低酸性飲料の濃度は、その最終濃度すなわち希釈されて最終の調合工程が行われる時の濃度に対して高濃度であることが必要である。高濃度の低酸性飲料に重曹を添加することによって、短時間で効率よく重曹溶液を低酸性飲料に分散することが可能となり、炭酸ガスがイオン化して残留せずにガス状となって発泡することにより除去することが可能となる。重曹を添加する前の低酸性飲料の濃度は希釈後の濃度の2倍以上であることが好ましく、2.5倍以上であることがより好ましい。 The pH of low-acid beverages such as coffee beverages and tea beverages before adding sodium bicarbonate is usually 6 or less. And in order to efficiently produce a low-acid beverage that achieves the object of the present invention, the concentration of the low-acid beverage before adding baking soda is the final concentration, that is, the concentration at which the final preparation step is performed after dilution. It is necessary to have a high concentration. By adding baking soda to highly concentrated low-acid beverages, it becomes possible to efficiently disperse the baking soda solution in the low-acid beverages in a short time, and carbon dioxide gas ionizes and foams in a gaseous form without remaining. Can be removed. The concentration of the low-acid beverage before adding sodium bicarbonate is preferably at least twice the concentration after dilution, more preferably at least 2.5 times.
また重曹を添加するときの低酸性飲料は高温状態であることが必要である。飲料が高温状態にあることにより、高濃度の低酸性飲料と重曹の反応が著しく増進され、飲料のpH調整や炭酸ガスの発泡、除去が促進される。このため重曹を添加するときの低酸性飲料の温度は50℃以上が好ましく、60℃以上がより好ましく、70℃以上が最も好ましい。 Moreover, the low-acid drink at the time of adding sodium bicarbonate needs to be in a high temperature state. When the beverage is in a high temperature state, the reaction between the high-concentration low-acid beverage and baking soda is remarkably enhanced, and the pH adjustment of the beverage and the foaming and removal of carbon dioxide gas are promoted. For this reason, the temperature of the low acid beverage when adding baking soda is preferably 50 ° C. or higher, more preferably 60 ° C. or higher, and most preferably 70 ° C. or higher.
また飲料のpH調整や炭酸ガスの発泡、除去を効率的に実現するには、重曹の添加は低酸性飲料を高速で攪拌しながら短時間で添加することがこのましい。攪拌速度や重曹の添加時間は低酸性飲料の調合タンクの容量や攪拌手段によって異なるので一概に決定できないが、所与の条件の下で飲料をできるだけ高速で攪拌し、重曹をできるだけ短時間で飲料に添加することが望ましい。 In order to efficiently adjust the pH of the beverage and foam and remove carbon dioxide, it is preferable to add sodium bicarbonate in a short time while stirring the low-acid beverage at high speed. Stirring speed and addition time of baking soda vary depending on the capacity of the low-acid beverage blending tank and the stirring means, so it cannot be determined in general, but under the given conditions, the beverage is stirred as fast as possible and the baking soda is drinked in the shortest possible time. It is desirable to add to.
こうして高濃度、高温状態の低酸性飲料に重曹を添加した後しばらくの間攪拌を続けることにより、重曹からの炭酸ガスを発泡させ、低酸性飲料から除去する。飲料から炭酸ガスが充分に除去されたら攪拌を終了し、低酸性飲料に純水を加えて最終濃度に希釈し、冷却した後
最終の調合工程を行う。調合工程においては、乳成分(全粉乳、脱脂粉乳等)や砂糖、乳化剤、香料等の添加剤を添加して低酸性飲料の調合を完了する。調合を完了した低酸性飲料は充填装置に送り、プラスチックボトル、プラスチックカップ、金属缶等の容器に常法により充填し、密封して製品とする。
In this way, by adding baking soda to the high-concentration, high-temperature, low-acid beverage, stirring is continued for a while, so that carbon dioxide gas from the baking soda is foamed and removed from the low-acid beverage. When the carbon dioxide is sufficiently removed from the beverage, the stirring is terminated, and pure water is added to the low-acid beverage to dilute to the final concentration, and after cooling, the final blending step is performed. In the blending process, additives such as milk components (whole milk powder, skimmed milk powder, etc.), sugar, emulsifiers, flavors and the like are added to complete the blending of the low acid beverage. The low-acid beverage after completion of preparation is sent to a filling device, filled in a container such as a plastic bottle, plastic cup, or metal can by a conventional method, and sealed to obtain a product.
重曹由来の炭酸の特性を確かめるため、テーブルテストを実施した。
〔サンプル液中の炭酸ガス濃度の測定法〕
サンプル液中の炭酸濃度測定には東興化学研究所製の炭酸ガス濃度測定器(Ti−9004)を用いた。なお、炭酸はガスの状態とイオンの状態で溶解しており、pH調整を行わないで測定した値(補正値=実測値/1.1)を炭酸ガス状態での溶解濃度(Cgas)、pHを4以下に調整して測定した値を総炭酸濃度(Call)として評価した。これらにより、イオンとして溶解している濃度(Cion)は
Cion=Call−Cgas
として求められる。濃度はすべてCO2換算値で評価した。また、サンプル液が本装置の適正使用濃度範囲(2〜440mg/L)を超える濃度の場合にはサンプル液を希釈して測定し、測定値を希釈倍率で補正して用いた。温度が高い場合には、サンプル液を炭酸ガスが逃げないように密封した状態で、氷水で急冷し、室温にしてから測定した。
A table test was conducted to confirm the characteristics of carbonic acid derived from baking soda.
[Method for measuring carbon dioxide concentration in sample solution]
For measuring the carbonic acid concentration in the sample solution, a carbon dioxide concentration measuring device (Ti-9004) manufactured by Toko Chemical Laboratory was used. Carbonic acid is dissolved in a gas state and an ion state, and a value (correction value = actual value / 1.1) measured without adjusting pH is a dissolved concentration (Cgas), pH in the carbon dioxide state. Was adjusted to 4 or less, and the measured value was evaluated as the total carbonic acid concentration (Call). As a result, the concentration dissolved as ions (Cion) is Cion = Call-Cgas.
As required. All concentrations were evaluated in terms of CO2. Further, when the concentration of the sample liquid exceeded the proper use concentration range (2 to 440 mg / L) of the present apparatus, the sample liquid was diluted and measured, and the measured value was corrected by the dilution factor. When the temperature was high, the sample solution was sealed so that the carbon dioxide gas would not escape, and then quenched with ice water and brought to room temperature.
(1)重曹溶液での確認
重曹は一般に水溶液の状態で添加される。そこで、重曹由来の炭酸ガスの低減に有効と思われることから、以下のように重曹を熱湯に溶解し、溶存総炭酸濃度の経時変化を評価した。
(1) Confirmation with sodium bicarbonate solution Sodium bicarbonate is generally added in the form of an aqueous solution. Therefore, since it seems to be effective in reducing carbon dioxide gas derived from baking soda, sodium bicarbonate was dissolved in hot water as follows, and the change over time in the total dissolved carbonic acid concentration was evaluated.
加熱したイオン交換水を2リットル用のフラスコに900g投入し、攪拌しながら重曹100gを投入して10重量%重曹溶液を作成した。この溶液中の溶存炭酸ガス量の経時変化を投入1分後から30分後まで評価した。なお、重曹溶液はホットスターラーと保温材とで保温し、スターラーの回転数は200rpmとした。また、重曹を投入する直前のイオン交換水の温度は85℃で、投入直後は77℃、30分後の評価終了時は79℃で、重曹添加後の評価液の温度はほぼ一定に保たれていた。 900 g of heated ion-exchanged water was put into a 2 liter flask, and 100 g of sodium bicarbonate was added while stirring to prepare a 10 wt% sodium bicarbonate solution. The time-dependent change in the amount of dissolved carbon dioxide in the solution was evaluated from 1 minute to 30 minutes after the addition. The baking soda solution was kept warm with a hot stirrer and a heat insulating material, and the rotation speed of the stirrer was 200 rpm. The temperature of ion-exchanged water immediately before adding sodium bicarbonate was 85 ° C, 77 ° C immediately after adding sodium bicarbonate, 79 ° C at the end of evaluation after 30 minutes, and the temperature of the evaluation solution after adding sodium bicarbonate was kept almost constant. It was.
10重量%重曹溶液中の理論上の総炭酸濃度は5.2重量%であるが、溶解直後から、測定値はほぼ95%以上の残存率を示し、ほとんど減少することはなく、重曹溶液の状態での炭酸ガスの低減は期待できないことが判った。 The theoretical total carbonic acid concentration in the 10% by weight sodium bicarbonate solution is 5.2% by weight, but immediately after dissolution, the measured value shows a residual ratio of almost 95% or more and hardly decreases. It was found that reduction of carbon dioxide in the state cannot be expected.
(2)高濃度コーヒー液での確認(温度・攪拌・時間・濃度の効果)
1リットル用のビーカに加熱したイオン交換水とコーヒーエキスを入れ、攪拌して高濃度コーヒー液を所定量作成し、表1に示す所定の温度に調整した。この高濃度コーヒー液を攪拌しながら重曹溶液を所定量投入してpHを調整した。なお、高濃度コーヒー液はホットスターラーと保温材とで保温し、スターラーの回転数は1000rpmを基準として500rpm、250rpmとした。また、pH調整直後の高濃度コーヒー液の温度はほぼ80℃、70℃、50℃、25℃となるように調整した。実験例の実験条件を表1に示す。
(2) Confirmation with high-concentration coffee liquid (effect of temperature, stirring, time, concentration)
Heated ion-exchanged water and coffee extract were put into a 1-liter beaker, and a predetermined amount of high-concentration coffee liquid was prepared by stirring and adjusted to a predetermined temperature shown in Table 1. While stirring the high-concentration coffee liquid, a predetermined amount of a sodium bicarbonate solution was added to adjust the pH. The high-concentration coffee liquid was kept warm with a hot stirrer and a heat-retaining material, and the rotation speed of the stirrer was 500 rpm and 250 rpm with 1000 rpm as a reference. The temperature of the high-concentration coffee liquid immediately after pH adjustment was adjusted to approximately 80 ° C., 70 ° C., 50 ° C., and 25 ° C. Table 1 shows the experimental conditions of the experimental example.
重曹溶液は75℃に保持し用いた。
The sodium bicarbonate solution was used at 75 ° C.
高濃度コーヒー液に重曹溶液を添加すると泡立つが、高濃度コーヒー液の温度が高いほど(実験例1)、また70℃での実験例でみると、強く撹拌しているほど(実験例2)、泡立ちは顕著であった。また、泡立ちが顕著であるほど、泡の消失時間も早いことが判った。逆に温度が低い場合(実験例6)や撹拌が弱い場合(実験例4)は、泡は短時間に発生しなく、長時間に渡って発生した。これらのことから、高温で強く撹拌した方が、炭酸ガスが発生する反応が早く進むことが判った。 When the baking soda solution is added to the high-concentration coffee liquor, bubbles are formed. The foaming was remarkable. Moreover, it turned out that the foam | bubble disappearance time is so early that foaming is remarkable. On the contrary, when the temperature was low (Experimental Example 6) or when the stirring was weak (Experimental Example 4), bubbles did not occur in a short time, but occurred for a long time. From these facts, it was found that the reaction in which carbon dioxide gas is generated proceeds faster when the mixture is stirred strongly at a high temperature.
各実験例について、高濃度コーヒー液のpHおよび炭酸ガス濃度を評価した。図2に温度の効果(実験例1・2・5・6)、図3に撹拌の効果(実験例2・3・4)、図4に重曹添加後の経過時間の効果(実験例7)を示す。なお、評価は泡が消失したことを確認した後に実施した。また、重曹溶液を添加する前のpHは4.65であった。 For each experimental example, the pH and carbon dioxide concentration of the high-concentration coffee liquor were evaluated. FIG. 2 shows the effect of temperature (Experimental Examples 1, 2, 5 and 6), FIG. 3 shows the effect of stirring (Experimental Examples 2, 3, and 4), and FIG. 4 shows the effect of elapsed time after the addition of sodium bicarbonate (Experimental Example 7). Indicates. The evaluation was performed after confirming that the bubbles disappeared. The pH before adding the sodium bicarbonate solution was 4.65.
図2・図3・図4のように、温度が高い程、強く攪拌する程、時間を長くする程、総炭酸濃度は低下することが判った。また、総炭酸濃度の低下とともにpHが上昇し、同時に単一分子としての溶存炭酸ガス濃度も低下することが判った。なお、重曹の添加はpHの調整にあることから、pHが必要以上に上昇する場合には、重曹の添加量を適宜調整すればよいことが判った。 2, 3, and 4, it was found that the higher the temperature, the stronger the stirring, and the longer the time, the lower the total carbonic acid concentration. Moreover, it turned out that pH raises with the fall of a total carbonic acid concentration, and the dissolved carbon dioxide gas concentration as a single molecule also falls simultaneously. In addition, since addition of baking soda exists in adjustment of pH, when pH rose more than needed, it turned out that what is necessary is just to adjust the addition amount of baking soda suitably.
なお、コーヒー飲料において、フレーバー保持の点からすると、高温で時間を長くすることはあまり好ましくない。そこで、実験例1〜7では高濃度コーヒー液の濃度を製品時に5倍希釈する濃度としたが、次にコーヒーエキスの濃度を変えて、実施例7と同様の実験を行った(実験例8・9・10)。図5に重曹添加後の炭酸ガス濃度とpHの推移を示す。なお、図5ではコーヒーエキスの濃度が異なるため、縦軸は重曹由来の総炭酸濃度に対する残存率で示した。 In coffee beverages, from the viewpoint of flavor retention, it is not preferable to increase the time at a high temperature. Therefore, in Experimental Examples 1 to 7, the concentration of the high-concentration coffee liquor was set to a concentration that was diluted 5 times at the time of the product.・ 9 ・ 10). FIG. 5 shows changes in carbon dioxide concentration and pH after the addition of sodium bicarbonate. In FIG. 5, since the coffee extract concentration is different, the vertical axis represents the residual rate relative to the total carbonic acid concentration derived from baking soda.
図5から分かるように、高濃度コーヒー液の濃度が高い程、短時間に炭酸ガス濃度を低減できることが判った。ただし、時間が10分程度経つと差は認められなくなった。 As can be seen from FIG. 5, it was found that the higher the concentration of the high-concentration coffee liquor, the shorter the carbon dioxide concentration can be reduced. However, no difference was observed after about 10 minutes.
以上の実験から、重曹溶液での炭酸ガス濃度の低減は難しく、高濃度コーヒー液の濃度および温度が高い状態で高速で攪拌することが持込の炭酸ガス濃度の低減を短時間に達成する上で効果的であることが判った。なお、温度を高くした場合の効果は、高濃度コーヒー液に重曹を添加したときの炭酸ガスの発生反応を速める効果と、炭酸ガスの溶解を防止する効果、泡の消泡効果、炭酸ガスの除去に効果することが明らかとなった。また、強い攪拌と高濃度コーヒー液の濃度を上げる効果は、炭酸ガスの発生反応を速める効果にあること考えられる。すなわち、スケールアップした実際の調合では、温度・攪拌・時間・濃度が更に顕著に効果ないし影響すると考えられる。次に実施例により確認した。 From the above experiments, it is difficult to reduce the carbon dioxide concentration in the baking soda solution. Stirring at high speed while the concentration and temperature of the high-concentration coffee liquor is high can achieve a reduction in the concentration of carbon dioxide brought in in a short time. And found to be effective. The effects of increasing the temperature include the effect of accelerating the carbon dioxide gas generation reaction when baking soda is added to the high-concentration coffee liquor, the effect of preventing the dissolution of carbon dioxide gas, the defoaming effect of bubbles, It became clear that it was effective for removal. Moreover, it is thought that the effect which raises the density | concentration of strong stirring and a high concentration coffee liquid has the effect of accelerating | stimulating the carbon dioxide generation reaction. That is, in actual scaled-up preparation, it is considered that temperature, stirring, time, and concentration are more remarkably effective or affected. Next, it confirmed by the Example.
[プラスチック容器]
1.プラスチックカップ
(外面側)ポリプロピレン(630μm)/接着剤層(30μm)/エチレン−ビニルアルコール共重合体(180μm)/接着剤層(30μm)/ポリプロピレン(630μm)(内面側)の多層プラスチックシート(1.5mm)を真空成形し、開口部にフランジ部を形成した側壁がテーパー状で満注内容量225mlのプラスチックカップを製造した。
上記プラスチックカップの各部分の寸法は、フランジ外径76mm、開口部内径73mm、底部径48mm、高さ94mmとした。
[Plastic container]
1. Plastic cup (outer side) polypropylene (630 μm) / adhesive layer (30 μm) / ethylene-vinyl alcohol copolymer (180 μm) / adhesive layer (30 μm) / polypropylene (630 μm) (inner side) multilayer plastic sheet (1 0.5 mm) was vacuum-formed, and a plastic cup having a full inner capacity of 225 ml with a tapered side wall with a flange formed at the opening was manufactured.
The dimensions of each part of the plastic cup were a flange outer diameter of 76 mm, an opening inner diameter of 73 mm, a bottom diameter of 48 mm, and a height of 94 mm.
2.シール材
下層からポリプロピレンフィルム(30μm)/接着層(3μm)/アルミ箔(20μm)/接着層(4μm)/二軸延伸ポリエチレンテレフタレートフィルム(12μm)から成る多層フィルムをシール材として用いた。
2. Sealing material A multilayer film comprising a polypropylene film (30 μm) / adhesive layer (3 μm) / aluminum foil (20 μm) / adhesive layer (4 μm) / biaxially stretched polyethylene terephthalate film (12 μm) from the lower layer was used as the sealing material.
[評価]
1.ヘッドスペースの炭酸ガス量
pH 4以下にした25℃の飽和食塩水中にて、ヘッドスペースガス量を捕集し、その体積を評価した。また、ガスクロマトグラフィーにより、炭酸ガス濃度を測定し、ヘッドスペースガスから炭酸ガス量を求めた。なお、評価は1条件について3カップずつ行い、平均値を評価した。
[Evaluation]
1. The amount of carbon dioxide in the headspace The amount of headspace gas was collected in a saturated saline solution at 25 ° C. adjusted to pH 4 or less, and the volume was evaluated. Further, the carbon dioxide concentration was measured by gas chromatography, and the amount of carbon dioxide was determined from the headspace gas. In addition, evaluation was performed 3 cups per condition, and the average value was evaluated.
2.ホットウォーマー試験
(株)タニックス製のペットボトルウォーマー(DC−P75)における過酷加温条件として速熱モードがある。これは低温の容器が一度に大量に投入された場合に、熱板を高温設定に切り換えるもので、80分間継続する。この速熱モードでの加熱された後、容器底部が膨らみ、座りが悪くなったものを不良とした。また、蓋材のヒートシール部が後退したもの、および密封不良となったものを不良とした。なお、n数は3カップとした。
2. Hot warmer test
There is a rapid heating mode as a severe heating condition in a PET bottle warmer (DC-P75) manufactured by Tanix Co., Ltd. This is to switch the hot plate to the high temperature setting when a large number of low temperature containers are charged at once, and it continues for 80 minutes. After heating in this rapid heating mode, the bottom of the container swelled and became poorly seated. Moreover, the thing which the heat seal part of the lid | cover material retreated and the thing which became poor in sealing was made into the defect. The n number was 3 cups.
[実施例1]
90℃に保持した熱水15.3kgが入った、200rpmの条件で高速撹拌している50Lの保温機能付きの調合タンクに、3.2kgのエキス(濃縮コーヒー抽出液)を投入した。エキスが均一に希釈された後の高濃度コーヒー液の温度は75℃、pHは4.6であった。これに75℃の10重量%重曹溶液1.5kgを一気に投入した。投入後、高濃度コーヒー液は泡立ち、泡は2〜3分で消失した。そのまま5分間攪拌し、重曹由来の炭酸ガスを除去した後、イオン交換水で上記コーヒー液を4倍に希釈しながら25℃に冷却し、200Lタンクに供給した。これに攪拌しながらグラニュー糖と生乳とを加えて溶解した後、最終的に5倍希釈となるように調整して、ミルク入りコーヒー飲料とした。
このミルク入りコーヒー飲料を60℃に加温して、上記プラスチックカップに180g充填後、ヘッドスペースを窒素ガス75%と炭酸ガス25%の混合ガスでガス置換を行い、カップ容器のフランジ部に上記シール材をヒートシールしてプラスチック容器から成る容器詰め低酸性飲料を製造し、125℃−15分(F0=35)のレトルト殺菌を施した。
レトルト殺菌後の上記容器詰め低酸性飲料を評価した結果を表2に示す。
[Example 1]
3.2 kg of extract (concentrated coffee extract) was charged into a 50 L heat-stabilized mixing tank containing 15.3 kg of hot water maintained at 90 ° C. and stirred at a high speed of 200 rpm. The temperature of the high-concentration coffee liquid after the extract was diluted uniformly was 75 ° C. and the pH was 4.6. To this, 1.5 kg of a 10% by weight sodium bicarbonate solution at 75 ° C. was charged all at once. After charging, the high-concentration coffee liquor foamed and the foam disappeared in 2 to 3 minutes. The mixture was stirred for 5 minutes to remove the carbon dioxide gas derived from baking soda, and then cooled to 25 ° C. while diluting the coffee liquid four times with ion-exchanged water, and supplied to a 200 L tank. While stirring, granulated sugar and raw milk were added and dissolved, and finally adjusted to a 5-fold dilution to obtain a coffee drink with milk.
This milk-containing coffee drink is heated to 60 ° C., and 180 g is filled in the plastic cup. Then, the head space is replaced with a mixed gas of 75% nitrogen gas and 25% carbon dioxide gas, and the flange portion of the cup container The sealing material was heat-sealed to produce a container-filled low-acid beverage comprising a plastic container, and subjected to retort sterilization at 125 ° C. for 15 minutes (F0 = 35).
Table 2 shows the results of evaluating the container-packed low-acid beverage after retort sterilization.
[実施例2]
実施例1において、調合したミルク入りコーヒーを熱交換機を用いて、145℃−9秒の殺菌を施し、25℃に冷却した状態で、予め薬剤滅菌したプラスチックカップおよび蓋材を用いた以外は、同様に容器詰め低酸性飲料を製造して評価した。
[Example 2]
In Example 1, the prepared milk-containing coffee was sterilized at 145 ° C. for 9 seconds using a heat exchanger, and cooled to 25 ° C., except that a plastic cup and lid material preliminarily sterilized with a drug were used. Similarly, a container-packed low-acid beverage was produced and evaluated.
[実施例3]
実施例1において、調合したミルク入りコーヒーの充填温度を70℃、ヘッドスペースのガス置換を窒素ガスのみで行った以外は、同様に容器詰め低酸性飲料を製造して評価した。
本実施例では、ヘッドスペースのガス置換において、混合ガス由来の炭酸ガスが存在しないため、容器内の総炭酸量は実施例1よりも減少した。
[Example 3]
In Example 1, a container-filled low-acid beverage was produced and evaluated in the same manner except that the filling temperature of the blended coffee with milk was 70 ° C. and the headspace was replaced with nitrogen gas alone.
In this example, since carbon dioxide derived from the mixed gas does not exist in the head space gas replacement, the total amount of carbonic acid in the container was smaller than that in Example 1.
[比較例1]
実施例1において、高濃度コーヒー液の濃度を最終製品の段階で1.5倍に希釈する条件とした以外は、同様に容器詰め低酸性飲料を製造して評価した。なお、濃度(希釈倍率)を変えたことにより、調合タンクには100Lの保温機能付きのものを用い、配合は熱水62kg(85℃)、エキス3.2kg、10重量%重曹溶液1.5kg(75℃)とした。
pH調整では、実施例1と同条件で攪拌したが、容量が増した分、重曹溶液の混ざりは悪く、泡立ちは少ないが添加後5分経過しても泡が発生していた。
[Comparative Example 1]
In Example 1, a container-packed low-acid beverage was produced and evaluated in the same manner except that the concentration of the high-concentration coffee liquid was changed to 1.5 times at the final product stage. In addition, by changing the concentration (dilution ratio), a mixing tank with a 100 L heat-retaining function was used, and the blending was 62 kg (85 ° C.) of hot water, 3.2 kg of extract, 1.5 kg of 10 wt% sodium bicarbonate solution. (75 ° C.).
In pH adjustment, stirring was performed under the same conditions as in Example 1. However, the amount of the sodium bicarbonate solution was poor due to the increase in volume, and foaming was small, but foaming occurred even after 5 minutes had elapsed after addition.
[比較例2]
実施例1において、高濃度コーヒー液の温度を25℃、貯蔵タンク内のコーヒー液を撹拌せずに重曹溶液を添加した以外は、同様に容器詰め低酸性飲料を製造して評価した。
pH調整では、実施例1と同条件で攪拌したが、高濃度コーヒー液の温度は30℃以下であり、重曹溶液の混ざりはよいものの、添加後の泡立ちは少ないが5分経過しても泡が発生していた。
[Comparative Example 2]
In Example 1, the container-packed low-acid beverage was similarly produced and evaluated except that the temperature of the high-concentration coffee liquid was 25 ° C. and the baking soda solution was added without stirring the coffee liquid in the storage tank.
In the pH adjustment, stirring was performed under the same conditions as in Example 1. However, although the temperature of the high-concentration coffee liquid was 30 ° C. or less and mixing of the baking soda solution was good, foaming after addition was small, but foaming occurred even after 5 minutes. Had occurred.
[比較例3]
実施例1において、グラニュー糖と生乳とを加える直前に、すなわち25℃下の低濃度のコーヒー液の状態(希釈状態)で、低速回転でpH調整した以外は、同様に容器詰め低酸性飲料を製造して評価した。
[Comparative Example 3]
In Example 1, just before adding granulated sugar and raw milk, that is, in the state of low-concentration coffee liquid at 25 ° C. (diluted state), except that the pH was adjusted by low-speed rotation, a container-packed low-acid beverage was similarly prepared. Manufactured and evaluated.
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JPH11342918A (en) * | 1998-03-30 | 1999-12-14 | Toyo Seikan Kaisha Ltd | Manufacture of container-stuffed food |
JP2003063571A (en) * | 2002-06-12 | 2003-03-05 | Coca Cola Asia Pacific Kenkyu Kaihatsu Center:Kk | Method for providing heated beverage |
WO2008139725A1 (en) * | 2007-05-08 | 2008-11-20 | Kao Corporation | Concentrate composition for drink from concentrate |
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JPH11342918A (en) * | 1998-03-30 | 1999-12-14 | Toyo Seikan Kaisha Ltd | Manufacture of container-stuffed food |
JP2003063571A (en) * | 2002-06-12 | 2003-03-05 | Coca Cola Asia Pacific Kenkyu Kaihatsu Center:Kk | Method for providing heated beverage |
WO2008139725A1 (en) * | 2007-05-08 | 2008-11-20 | Kao Corporation | Concentrate composition for drink from concentrate |
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