JP3585689B2 - Method and apparatus for continuously blending beverage products - Google Patents
Method and apparatus for continuously blending beverage products Download PDFInfo
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Description
【0001】
【発明の属する技術分野】
一般的に飲料製品は、規定の成分分量で調合された液体を殺菌、充填、包装の各工程を経て製造される。
本発明は、粉体、固体、液体を原料としてこれ等を個別に制御して、連続的に規定の製品を混合且つ溶解させて飲料製品を得るための連続調合方法およびその装置に関する。
【0002】
【従来の技術】
乳製品や清涼飲料水等飲料製品は、幾種類かの原料を調合することにより製造が開始される。たとえば加工乳と言われる製品は、バター、クリーム、脱脂粉乳、水と言った原料が混合されたものであり、また清涼飲料水は、グラニュー糖、液糖、濃縮果汁、安全剤、純水がその主要原料となっているものである。
【0003】
そして、上記した加工乳や清涼飲料水等飲料製品は、図2に示すフローチャートのような流れで行われる。すなわち、
各原料は、大きな調合タンク1に投入され、攪拌エネルギーにより分散、混合溶解されて、高濃度の一次調合液(濃縮調合液)となる。こ濃縮調合液は、次の貯蔵タンク2に送られ、ここで水で希釈されて、製品として調合液となり、貯蔵タンク2毎に成分検査が行われ、次の殺菌機3による殺菌工程に送られる。
【0004】
通常、調合タンク1は2基設置されており、1時間程度で1バッチの調合が完了し、交互に調合タンクを使用して連続的に調合作業が進められる(バッジ連続)。
各バッチに投入する固体原料7および粉体原料8は、予め計量されているが、多種の原料がある場合には非常に煩瑣で専用評料工程(原料秤量室4)が必要になる。また、これ等の多量のは固体原料7、粉体原料8は、袋、ポリ容器、ガラス容器等に収納した状態で調合タンク1の上部にある原料投入口5の近くに設けられた高い作業台6まで担ぎ上げる必要があり、しかも多大の労力を使って調合タンク1の原料投入口5から投入する必要があった。また、このように人手を介していることが原因で原料の未投入や異物混入等が不本意にも起きている。
尚、液体原料はタンク9から送入されてふぃる。また図中符号10はポンプを示す。
【0005】
品種が多く製造量の多い工場では、調合タンク1の本数も必然的に多くなる。たとえば当日殺菌する調合液が入っている貯蔵タンクと、翌日殺菌する調合液を貯めるために当日調合する貯蔵タンクとが必要になり、合計で当日使用分の2倍のタンク本数が設置される。
【0006】
食品工場においては、タンク内面およびパイプラインは毎日洗浄される。このためにタンク本数やパイプラインの数が多くなると、その分洗浄にかかるエネルギー、時間のロスも多くなる。
【0007】
【発明が解決しようとする課題】
本発明は、上記したような現状に鑑み、イニシャルコスト・エネルギーコスト・メンテナンスコスト・管理コスト等の低減化、タンクの削減化、配管の削減化、設置面積の縮少化、洗浄装置の系統数の少減化、立ち上がり時間の短縮化、設備費用の低減化、人手作業の削減化、トラブルの少減化、およびエネルギーや時間のロスの解消等を達成できる新規の飲料製品の連続調合方法およびその装置を提供することを目的とするものである。
【0008】
【課題を解決するための手段】
上記目的を達成するために本発明は、冷蔵・冷凍の油脂をベースにした固体原料を連続粉砕機と加熱ヒーターにより液状化してからタンクに保存する工程と液体原料を別のタンクに保存する工程と多数種の粉体原料を更に別のタンクに個別に保存する工程と微量原料液を別のタンクに製造保存する工程とを別々に制御すると共に上記タンクから各粉体原料を定量粉体切り出し機を介して種類ごとに受けてこれを仕込み水やミルク等液体と均一に分散混合して混合液を連続して得る工程を行い、次いで上記液状化固体原料と液体原料と微量原料液と粉体原料混合液とを液体ブレンドユニット部により連続して比率混合する工程を行うことを特徴とするものであり、
また、冷蔵・冷凍の油脂をベースにした固定原料を連続粉砕機および加熱ヒーターにより液状化して保存するための固体原料貯蔵部と、液体原料を保存するための液体原料貯蔵部と、多数種の粉体原料を個別に保存するための粉体原料貯蔵部と、粉体原料貯蔵部から定量粉体切り出し機を介して受けてこれと仕込み水やミルク等液体との混合液を連続して得るための粉体連続分散混合ユニット部と、微量原料液を保存していて要求に応じて供給するための微量原料液供給部と、上記液状化固体原料と液体原料と微量原料液と粉体原料混合液を上記各部より受けてこれ等を連続して混合均一化するための液体ブレンドユニット部と、を備えたことを特徴とするものである。
【0009】
【実施例】
本発明の実施例を図1に依拠して説明する。すなわち、
本発明は、固体原料貯蔵部11と、液体原料貯蔵部12と、粉体原料貯蔵部13と、粉体連続分散混合ユニット部14と、微量原料液供給部15と、液体ブレンドユニット部16と、を備えているものであって、次に各部を説明する。
【0010】
固体原料貯蔵部11;冷蔵・冷凍の油脂をベースにした固体原料21は、連続粉砕機22と加熱ヒーター23によって液状化され、貯蔵用タンク24に保存される。
【0011】
液体原料貯蔵部12;ローリー26からの液体原料を貯蔵用タンク27に移送して保存する。
【0012】
粉体原料貯蔵部13; 粉体原料については、各工場でその種類、使用量、荷姿により物流システムに違いがあるが、ここでは1日分または1ロット分の粉体原料(荷姿は20〜25kgの袋)28を自動解体機29により解体し、空気輸送にて貯蔵用タンク30、31に移送るする。
種類として、全脂粉乳、脱脂粉乳、乳化剤安定剤および砂糖などがある。
砂糖については、1トンのタイコン32を吊り上げて貯槽33に投入する。
これ等、粉体の解体・輸送・貯槽については、自動解体機の導入と輸送システムの自動化により無人化・省力化・労働集約化が可能であるが、粉体消費量の少ない、小中工場では、手動レベルの設備でもよい。
【0013】
粉体連続分散混合ユニット部14;粉体貯蔵用タンクすなわち、全脂粉乳貯蔵用タンク30・脱脂粉乳貯蔵用タンク31・砂糖貯槽33および手投入の安定貯槽34からスクリューフイーダーまたは空気輸送にて、粉体の種類ごとに設置された定量粉体切り出し機(定量フイダー)40〜43に搬送され、この定量フイダー40〜43から分散混合機44に供給される。
定量フイダー40〜43は、溶解液に対してある一定の重量%で粉体を連続して切り出して行くものである。尚、定量フイダー40〜43はロードセルタイプであって、粉体の見かけ比重が変化しても、切り出し重量を絶えず計測しコントロールしているために常に一定の切り出しを行うことが可能である。
各粉体の重量%はまちまちで、大体0.05%〜60%で溶解すれば調合液として十分な範囲を持つことができる。しかしこの範囲を1台の定量フィーダーでカバーすることはできないので、その粉体の調合液に対する重量%を調査して、能力を選定することになる。また定量フィーダーの可変範囲は、1:15(最小投入量:量大投入量)で設計され、切り出された粉体は、スクリウフィーダーにより、集合的に移送され、分散混合器に投入される。
更に粉体は、分散混合機44において、ヒーター45によつて暖められた液体(仕込みや水やミルク)と会合し、均一に分散混合された混合液となって連続的に送出される。
【0014】
微量原料液供給部15;多種類の微量・少量原料(粉体、液体)の処理に定量フィーダーや液体ブレンドユニットを利用することは、大きな投資金額が必要となり、品質的にも不安定になる等の問題がある。
これ等の問題に対して汎用的に対処するため、微量液体タンク45および移動タンク46で、多種類の微量・少量原料を秤量・溶解する。この秤量・溶解により調整された微量原料液は、液体ブレッドユニット部16の近くまで移動されて供給ライン47に接続される。これによるときには微量原料でも歩留りの良い状態で投入できる。
【0015】
液体ブレンドユニット部16;液体原料、粉体混合液及び多種類の微量・少量原料液および多種類の微量・少量原料液を合流管49およびスタテックミキサー50により比率混合させたのち均質機51にて溶解・予備乳化を行い、受けタンク52に貯蔵する。
そして、受けタンク52が殺菌機(図示せず)に送出する。
【0016】
【発明の効果】
本発明は、上記の通りであるので、これによれば イニシャルコスト・エネルギーコスト・メンテナンスコスト・管理コスト等の低減化、タンクの削減化、配管の削減化、設置面積の縮少化、洗浄装置の系統数の少減化、立ち上がり時間の短縮化、設備費用の低減化、人手作業の削減化、トラブルの少減化、およびエネルギーや時間のロスの解消等を充分に達成することが可能となるものであって、所期の目的を完全に達成できるという優れた効果を奏するものである。
【図面の簡単な説明】
【図1】本発明の実施例を示す全体のフローチャートである。
【図2】従来例を示す全体のフローチャートである。
【符号の説明】
1 調合タンク
2 貯蔵タンク
3 殺菌機
4 原料秤量室
5 原料投入口
6 作業台
7 固体原料
8 粉体原料
9 タンク
10 ポンプ
11 固体原料貯蔵部
12 液体原料貯蔵部
13 粉体原料貯蔵部
14 粉体連続分散混合ユニット部
15 微量原料液供給部
16 液体ブレンドユニット部
21 固体原料
22 連続粉砕機
23 加熱ヒーター
24 貯蔵用タンク
26 ローリー
27 貯蔵用タンク
28 袋入り粉体原料
29 自動解体機
30 全脂肪乳貯蔵用タンク
31 脱脂粉乳貯蔵槽
32 タイコン
33 砂糖貯槽
34 安定剤貯槽
40〜43 定量粉体切り出し機
44 分散混合機
45 ヒーター
46 移動タンク
47 供給ライン
49 合流管
50 スタテックミキサー
51 均質機
52 受けタンク
53 送りポンプ[0001]
TECHNICAL FIELD OF THE INVENTION
Generally, a beverage product is manufactured through a sterilization, filling, and packaging process of a liquid prepared in a prescribed component amount.
The present invention relates to a continuous dispensing method and apparatus for obtaining a beverage product by individually controlling powders, solids, and liquids as raw materials, and continuously mixing and dissolving prescribed products to obtain a beverage product.
[0002]
[Prior art]
BACKGROUND ART Beverage products such as dairy products and soft drinks are produced by preparing several types of raw materials. For example, a product called processed milk is a mixture of ingredients such as butter, cream, skim milk powder, and water, and soft drinks consist of granulated sugar, liquid sugar, concentrated fruit juice, safety agents, and pure water. It is the main raw material.
[0003]
Then, the above-described beverage products such as processed milk and soft drinks are performed according to the flow shown in the flowchart of FIG. That is,
Each raw material is put into a large preparation tank 1 and dispersed, mixed and dissolved by stirring energy to become a high concentration primary preparation liquid (concentrated preparation liquid). This concentrated preparation is sent to the
[0004]
Usually, two compounding tanks 1 are installed, and compounding of one batch is completed in about one hour, and compounding work is continuously performed alternately using the compounding tank (badge continuous).
The solid raw material 7 and the powder raw material 8 to be charged into each batch are measured in advance, but when there are various types of raw materials, it is very complicated and requires a dedicated evaluation process (raw material weighing chamber 4). These large amounts of solid raw material 7 and powder raw material 8 are stored in a bag, a plastic container, a glass container, or the like. It had to be carried up to the table 6 and moreover, it was necessary to use a large amount of labor to input the raw material from the raw material input port 5 of the mixing tank 1. Further, due to such manual operation, unfilled raw materials and inclusion of foreign substances are undesirably caused.
The liquid raw material is fed from the tank 9 and flows. Reference numeral 10 in the drawing indicates a pump.
[0005]
In a factory with many varieties and a large amount of production, the number of compounding tanks 1 is inevitably increased. For example, a storage tank containing the preparation liquid to be sterilized on the day and a storage tank prepared on the same day to store the preparation liquid to be sterilized on the next day are required, and a total of twice the number of tanks used on the day is installed.
[0006]
In food factories, tank interiors and pipelines are cleaned daily. For this reason, if the number of tanks or the number of pipelines increases, the energy and time required for cleaning increase accordingly.
[0007]
[Problems to be solved by the invention]
The present invention has been made in view of the above-mentioned situation, and has a reduction in initial cost, energy cost, maintenance cost, management cost, etc., a reduction in tanks, a reduction in piping, a reduction in installation area, a number of cleaning devices, A new method of continuously dispensing beverage products that can achieve a reduction in energy consumption, a reduction in startup time, a reduction in equipment costs, a reduction in manual work, a reduction in trouble, and a reduction in energy and time loss. It is intended to provide such a device.
[0008]
[Means for Solving the Problems]
In order to achieve the above object, the present invention provides a step of liquefying a solid raw material based on refrigerated / frozen fats and oils by a continuous pulverizer and a heater and then storing the solid raw material in a tank and a step of storing the liquid raw material in another tank And separately controlling the process of individually storing many kinds of powder raw materials in another tank and the process of manufacturing and storing a trace amount of raw material liquid in another tank, and cutting out each powder raw material from the above-mentioned tank in a fixed amount of powder. A process of receiving each type through a machine and dispersing and mixing the same with a liquid such as water or milk to obtain a mixed liquid continuously, and then the liquefied solid raw material, the liquid raw material, the trace raw material liquid and the powder It is characterized by performing a step of continuously mixing the body raw material mixed liquid with the liquid blending unit by a ratio,
In addition, a solid raw material storage unit for liquefying and storing fixed raw materials based on refrigerated / frozen fats and oils by a continuous pulverizer and a heater, a liquid raw material storage unit for storing liquid raw materials, A powder raw material storage unit for individually storing powder raw materials, and a mixed liquid of the powder raw material storage unit and a liquid such as water or milk which is received from the powder raw material storage unit via a fixed amount powder cutting machine and continuously obtained. A continuous powder mixing unit for storing the raw material liquid, a micro raw material liquid supply unit for storing and supplying a micro raw material liquid on demand, the liquefied solid raw material, the liquid raw material, the micro raw material liquid and the powder raw material And a liquid blending unit for receiving the mixed liquid from each of the above-mentioned parts and continuously mixing and homogenizing them.
[0009]
【Example】
An embodiment of the present invention will be described with reference to FIG. That is,
The present invention relates to a solid raw material storage unit 11, a liquid raw material storage unit 12, a powder raw material storage unit 13, a powder continuous dispersion mixing unit unit 14, a trace raw material liquid supply unit 15, a liquid blend unit unit 16, , And each unit will be described below.
[0010]
Solid raw material storage unit 11; Solid
[0011]
Liquid raw material storage unit 12; The liquid raw material from lorry 26 is transferred to
[0012]
Powder raw material storage unit 13: Regarding the powder raw material, there is a difference in the distribution system depending on the type, amount of use, and packing style at each factory. Here, the powder raw material for one day or one lot (packing style is 20 to 25 kg bag) 28 is dismantled by an automatic dismantling machine 29 and transferred to storage tanks 30 and 31 by pneumatic transportation.
Types include whole milk powder, skim milk powder, emulsifier stabilizers and sugar.
For sugar, 1 ton of tycon 32 is lifted and put into
For the dismantling, transportation and storage of powder, the introduction of an automatic dismantling machine and automation of the transport system can make it unmanned, labor-saving and labor intensive, but the Konaka Plant, which consumes less powder, Then, equipment of a manual level may be used.
[0013]
Powder continuous dispersion mixing unit unit 14; from a powder storage tank, that is, a tank 30 for storing whole milk powder, a tank 31 for storing skim milk powder, a
The quantitative feeders 40 to 43 are for continuously cutting out powder at a certain weight% with respect to the solution. Note that the quantitative feeders 40 to 43 are load cell types, and even if the apparent specific gravity of the powder changes, the cutout weight is constantly measured and controlled, so that a constant cutout can always be performed.
The weight% of each powder varies, and if it is dissolved in about 0.05% to 60%, a sufficient range can be obtained as a preparation liquid. However, since this range cannot be covered by one fixed-quantity feeder, the ability is selected by examining the weight% of the powder relative to the prepared liquid. The variable range of the fixed-quantity feeder is designed at 1:15 (minimum input amount: large input amount), and the cut-out powder is collectively transferred by a screw feeder and input into a dispersion mixer. .
Further, in the dispersion mixer 44, the powder is associated with the liquid (preparation, water or milk) warmed by the heater 45, and is continuously delivered as a uniformly dispersed mixed liquid.
[0014]
Use of a fixed amount feeder or a liquid blending unit for the processing of various kinds of small and small amounts of raw materials (powder and liquid) requires a large investment amount and is unstable in quality. There are problems such as.
In order to deal with these problems in general, a trace liquid tank 45 and a moving tank 46 measure and dissolve various kinds of trace and small amounts of raw materials. The trace raw material liquid adjusted by the weighing and dissolving is moved to the vicinity of the liquid bread unit 16 and connected to the supply line 47. In this case, even a small amount of raw material can be introduced in a good yield.
[0015]
Liquid blending unit 16; liquid raw material, powder mixed liquid, and various kinds of trace and small amount raw material liquids and various kinds of trace and small amount of raw liquid are mixed by means of a merging
And the receiving tank 52 sends out to a sterilizer (not shown).
[0016]
【The invention's effect】
Since the present invention is as described above, according to this, initial costs, energy costs, maintenance costs, management costs, etc. are reduced, tanks are reduced, piping is reduced, installation area is reduced, and a cleaning device is reduced. It is possible to sufficiently achieve the reduction of the number of systems, the shortening of the startup time, the reduction of equipment costs, the reduction of manual work, the reduction of troubles, and the elimination of energy and time loss. It is an excellent effect that the intended purpose can be completely achieved.
[Brief description of the drawings]
FIG. 1 is an overall flowchart showing an embodiment of the present invention.
FIG. 2 is an overall flowchart showing a conventional example.
[Explanation of symbols]
REFERENCE SIGNS LIST 1
Claims (2)
液体原料を別のタンクに保存する工程と、Storing the liquid material in a separate tank;
多数種の粉体原料を更に別のタンクに個別に保存する工程と、A step of individually storing many kinds of powder raw materials in still another tank,
微量原料液を別のタンクに製造保存する工程とを備え、上記各工程は夫々、独立して制御され、A step of manufacturing and storing the trace material liquid in a separate tank, wherein each of the above steps is independently controlled,
さらに、上記タンクから各粉体原料を定量粉体切り出し機を介して種類ごとに受けてこれを仕込み水やミルク等液体と均一に分散混合して混合液を連続して得る工程と、Further, a step of receiving each powder raw material from the tank through the quantitative powder cutout machine for each type, and uniformly dispersing and mixing this with a liquid such as water or milk to continuously obtain a mixed liquid,
上記混合液を連続して得る工程の後に、上記液状化固体原料と液体原料と微量原料液と粉体原料混合液とを液体ブレンドユニット部により連続して比率混合する工程とを有することを特徴とする飲料製品の連続調合方法。After the step of continuously obtaining the mixed liquid, a step of continuously mixing the liquefied solid raw material, the liquid raw material, the trace raw material liquid, and the powder raw material mixed liquid by a liquid blending unit unit in a ratio manner. Method for continuously blending beverage products.
液体原料を保存するための液体原料貯蔵部と、A liquid material storage unit for storing the liquid material,
多数種の粉体原料を個別に保存するための粉体原料貯蔵部と、A powder raw material storage unit for individually storing many types of powder raw materials,
粉体原料貯蔵部から定量粉体切り出し機を介して受けてこれと仕込み水やミルク等液体との混合液を連続して得るための粉体連続分散混合ユニット部と、A powder continuous dispersion mixing unit for receiving from the powder raw material storage unit via the quantitative powder cutting machine and continuously obtaining a mixed liquid thereof with a liquid such as charged water or milk,
微量原料液を保存していて要求に応じて供給するための微量原料液供給部と、A trace material liquid supply unit for storing the trace material liquid and supplying it on demand;
上記液状化固体原料と液体原料と微量原料液と粉体原料混合液を上記各部より受けてこれ等を連続して混合均一化するための液体ブレンドユニット部とを備え、A liquid blending unit for receiving the liquefied solid raw material, the liquid raw material, the trace raw material liquid, and the powder raw material mixed liquid from each of the parts and continuously mixing and homogenizing them,
上記粉体連続分散混合ユニット部において粉体が均一に分散混合された混合液を形成した後、上記液体ブレンドユニット部において各原料が混合された製品を作製することを特徴とする飲料製品の連続調合装置。After forming a liquid mixture in which the powders are uniformly dispersed and mixed in the powder continuous dispersion mixing unit, a product in which each raw material is mixed in the liquid blending unit is manufactured. Mixing device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP02716397A JP3585689B2 (en) | 1997-01-27 | 1997-01-27 | Method and apparatus for continuously blending beverage products |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP02716397A JP3585689B2 (en) | 1997-01-27 | 1997-01-27 | Method and apparatus for continuously blending beverage products |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH10201454A JPH10201454A (en) | 1998-08-04 |
| JP3585689B2 true JP3585689B2 (en) | 2004-11-04 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP02716397A Expired - Lifetime JP3585689B2 (en) | 1997-01-27 | 1997-01-27 | Method and apparatus for continuously blending beverage products |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| JP5809803B2 (en) * | 2011-01-11 | 2015-11-11 | 岩井機械工業株式会社 | Liquid product formulation manufacturing method |
| CN113662432B (en) * | 2021-09-27 | 2023-07-21 | 齐喝彩(常熟)信息科技有限公司 | Mixer of automatic beverage making machine |
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| JPH10201454A (en) | 1998-08-04 |
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