JPH04183376A - Heat sterilizing method - Google Patents
Heat sterilizing methodInfo
- Publication number
- JPH04183376A JPH04183376A JP2313771A JP31377190A JPH04183376A JP H04183376 A JPH04183376 A JP H04183376A JP 2313771 A JP2313771 A JP 2313771A JP 31377190 A JP31377190 A JP 31377190A JP H04183376 A JPH04183376 A JP H04183376A
- Authority
- JP
- Japan
- Prior art keywords
- pipe
- sterilized
- liquid
- solid article
- solids
- 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.)
- Granted
Links
- 230000001954 sterilising effect Effects 0.000 title claims abstract description 15
- 238000000034 method Methods 0.000 title claims description 11
- 239000007787 solid Substances 0.000 claims abstract description 29
- 239000007788 liquid Substances 0.000 claims abstract description 25
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 11
- 238000010438 heat treatment Methods 0.000 claims description 12
- 239000000463 material Substances 0.000 abstract description 8
- 230000001678 irradiating effect Effects 0.000 abstract description 4
- 235000013305 food Nutrition 0.000 abstract description 2
- 240000004713 Pisum sativum Species 0.000 description 4
- 235000010582 Pisum sativum Nutrition 0.000 description 4
- 230000014759 maintenance of location Effects 0.000 description 4
- 239000011343 solid material Substances 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 240000008042 Zea mays Species 0.000 description 2
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 2
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 2
- 235000015278 beef Nutrition 0.000 description 2
- 235000005822 corn Nutrition 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000011344 liquid material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000011345 viscous material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 244000000626 Daucus carota Species 0.000 description 1
- 235000002767 Daucus carota Nutrition 0.000 description 1
- 239000004278 EU approved seasoning Substances 0.000 description 1
- 244000061456 Solanum tuberosum Species 0.000 description 1
- 235000002595 Solanum tuberosum Nutrition 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000011194 food seasoning agent Nutrition 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 235000012015 potatoes Nutrition 0.000 description 1
- 235000015067 sauces Nutrition 0.000 description 1
- 235000014347 soups Nutrition 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
- Apparatus For Disinfection Or Sterilisation (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、固形物と液体の混合物から成る被殺菌物をパ
イプ中を連続的に移送しながら、マイクロ波を照射して
殺菌する方法に関する。Detailed Description of the Invention (Industrial Application Field) The present invention relates to a method for sterilizing an object consisting of a mixture of solid and liquid by irradiating it with microwaves while continuously transporting the object through a pipe. .
(従来の技術)
液体から成る被殺菌物をパイプ中を連続的に移送しなが
ら、マイクロ波を照射して殺菌する方法は公知であり、
実公昭63−5513号公報、特開昭62−11756
1号公報、特開昭63−111870号公報等に記載さ
れている。(Prior Art) A method of sterilizing a liquid object by irradiating it with microwaves while continuously transporting it through a pipe is known.
Utility Model Publication No. 63-5513, JP-A-62-11756
It is described in Publication No. 1, Japanese Unexamined Patent Publication No. 111870/1983, and the like.
これらの方法は、被殺菌物をパイプ中を移送しながら、
まずマイクロ波照射して高温にし、その後、断熱状態の
ホールディング部で殺菌に必要な時間高温に維持し、最
後に冷却して取り出すものである。These methods transport the material to be sterilized through the pipe.
First, it is heated to a high temperature by irradiation with microwaves, then maintained at high temperature for the time required for sterilization in an insulated holding section, and finally cooled and removed.
かかる殺菌方法は、原理上は加熱殺菌であり、十分な殺
菌効果を得るためにパイプ中を5分以上移送することを
必要とする。In principle, this sterilization method is heat sterilization, and in order to obtain a sufficient sterilization effect, it is necessary to transfer the material through a pipe for 5 minutes or more.
(発明が解決しようとする課題)
しかしながら、被殺菌物が液体の他に固形物を含む場合
、5分以上の時間パイプ中を移送する間に固形物が沈降
し、滞留してしまうという問題があった。(Problem to be Solved by the Invention) However, when the object to be sterilized contains solids in addition to liquids, there is a problem that the solids settle and stagnate while being transferred through the pipe for 5 minutes or more. there were.
そこで、本発明は、固形物と、液体の双方を含む被殺菌
物を、パイプ中を固形物が滞留することなく移送し、均
一にかつ充分殺菌する方法を提供することを目的とする
。SUMMARY OF THE INVENTION Therefore, an object of the present invention is to provide a method for uniformly and sufficiently sterilizing objects to be sterilized, including both solids and liquids, by transporting them through a pipe without the solids remaining therein.
(課題を解決するための手段)
この目的を解決するため、本発明は、径5〜20mmの
固形物と液体から成る被殺菌物をパイプ中を連続的に移
送しながら、バイブ周囲に順次設けられたマイクロ波加
熱装置及び断熱状態のホールディング部により加熱殺菌
する加熱殺菌方法において、液体が粘土2000cp以
上であることを特徴とする加熱殺菌方法を提供する。(Means for Solving the Problems) In order to solve this object, the present invention provides a method for sequentially disposing objects to be sterilized around a vibrator while continuously transporting objects to be sterilized consisting of solids and liquids having a diameter of 5 to 20 mm through a pipe. Provided is a heat sterilization method in which the liquid is sterilized by heat using a microwave heating device and a holding part in an adiabatic state, characterized in that the liquid is 2000 cp or more of clay.
(発明の詳細な
説明にかかる被殺菌物(1)は固形物と液体から成るも
のである。(The object to be sterilized (1) according to the detailed description of the invention consists of a solid substance and a liquid.
固形物としては食品が好ましく、通常5〜20mmのも
のである。例えば、角切の肉、グリーンピース、コーン
粒、キャロフト、ポテト等が例示できる。The solid material is preferably a food product, and usually has a size of 5 to 20 mm. For example, diced meat, green peas, corn kernels, carolft, potatoes, etc. can be used.
また、液体としては、各種調味斜入りのスープ、ホワイ
トソース等が使用できる。Further, as the liquid, soups with various seasonings, white sauce, etc. can be used.
かかる液体は2000cp以上の粘度を有することが必
要であ、好ましくは5000cp以上である。2000
cpより低い粘度の場合は、固形物が移送されずにパイ
プ中に滞留することがあるからである。同じく径10m
mのグリーンピース、同じく径10mmの角切キャロフ
ト、径10mmのコーン粒の沈降速度の実験例を第1表
に示す。Such a liquid needs to have a viscosity of 2000 cp or more, preferably 5000 cp or more. 2000
This is because if the viscosity is lower than cp, solids may not be transferred and may remain in the pipe. Also 10m in diameter
Table 1 shows an experimental example of the sedimentation rate of green peas of 1.5 mm, cubed carlofts of 10 mm in diameter, and corn grains of 10 mm in diameter.
第1表
かかる被殺菌物(1)は、第1図に示すように、パイプ
(4)端部に設けられたホンパー(2)から投入し、ポ
ンプ(3)によりバイブ〔4〕中を連続的に移送するこ
とができる。Table 1 As shown in Figure 1, the object to be sterilized (1) is introduced through the sieve (2) provided at the end of the pipe (4) and continuously passed through the vibrator [4] by the pump (3). can be transferred.
被殺菌物(1)を充分に加熱殺菌するため、パイプ(4
)の周囲には、順次、マイクロ波加熱装置(6)、ホー
ルディング部(7)が設ける必要がある。なお、固形物
と液体を均一に加熱殺菌するため、マイクロ波加熱装置
(6)の前に予備加熱装置(5)を配置することが望ま
しい。In order to sufficiently heat and sterilize the object to be sterilized (1), the pipe (4
), it is necessary to sequentially provide a microwave heating device (6) and a holding part (7). In addition, in order to uniformly heat and sterilize solids and liquids, it is desirable to arrange a preheating device (5) in front of the microwave heating device (6).
予備加熱装置(5)は熱交換方式によることが望ましい
、二〇熱交換方式による加熱においては、液体は、固形
物より加熱され易く、より高温になる。It is preferable that the preheating device (5) uses a heat exchange method. 20. In heating by a heat exchange method, liquids are more easily heated than solids and reach a higher temperature.
マイクロ波加熱装置(6)は、予備加熱された液体と固
形物を殺菌に必要な温度まで加熱するものである。固形
物は、予備殺菌装置(5)の加熱によって、液体より低
い温度に加熱されているが、マイクロ波による加熱効率
が良いことから、液体より高速度で昇温し、ホールディ
ング部(7)の入口で固形物と液体は略同−温度に達す
る。The microwave heating device (6) heats the preheated liquid and solid material to the temperature required for sterilization. The solids are heated to a lower temperature than the liquid by the pre-sterilizer (5), but because of the high heating efficiency of microwaves, the solids rise in temperature at a higher rate than the liquid, and the temperature of the holding part (7) increases. At the inlet, the solid and liquid reach approximately the same temperature.
予備加熱装置(5)は、例えば、パイプ(4)の周囲に
、大径のパイプを設け、加熱蒸気や熱水を通せば良い、
加熱蒸気や熱水等の熱媒体は、被殺菌物の移送方向とは
逆方向に、すなわちマイクロ波殺菌装置(6)側からパ
イプの入口に向かって通すことが、熱効率の点で好まし
い。The preheating device (5) may be configured by, for example, providing a large-diameter pipe around the pipe (4) and passing heated steam or hot water through it.
In terms of thermal efficiency, it is preferable that the heat medium such as heated steam or hot water be passed in the opposite direction to the direction of transfer of the object to be sterilized, that is, from the microwave sterilizer (6) side toward the entrance of the pipe.
かかる熱媒体は、被殺菌物(1)の種類によるが、70
〜100℃のものが好ましい、熱交換の時間は、160
から200秒を目安とすれば良い。Such a heat medium depends on the type of the object to be sterilized (1), but
The temperature of ~100°C is preferable, and the heat exchange time is 160°C.
A good guideline is 200 seconds.
マイクロ波加熱装置(6)は、パイプ外部からマイクロ
波を照射して、被殺菌物(1)自体の発熱を利用して殺
菌するものである。液体または粘稠体の温度が120〜
140℃となるように照射すれば良い。もっとも、固形
物の温度を基準にしても同様である6両者は、略同−温
度に達するからである。一般には、2.45(、Hzの
マイクロ波を、出力1.3Kwで、30〜90秒照射す
れば良い。The microwave heating device (6) sterilizes the object (1) by irradiating it with microwaves from outside the pipe and utilizing the heat generated by the object (1) itself. Temperature of liquid or viscous substance is 120~
It is sufficient to irradiate at a temperature of 140°C. However, even if the temperature of the solid material is taken as a standard, both of them reach approximately the same temperature. Generally, it is sufficient to irradiate microwaves of 2.45 Hz with an output of 1.3 Kw for 30 to 90 seconds.
ホールディング部(7)は、高温に達した被殺菌物(1
)を、殺菌に必要な時間、高温に維持するものである。The holding part (7) holds the object to be sterilized (1) which has reached a high temperature.
) is maintained at high temperature for the time required for sterilization.
パイプ(4)を断熱材料で被覆して設ければ良い。ホー
ルディングの時間は、10〜120秒で充分である。The pipe (4) may be provided by being covered with a heat insulating material. A holding time of 10 to 120 seconds is sufficient.
第1図に示すように、ホールディング部(7)で加熱殺
菌された被殺菌物(1)は、冷却部(8)を通過した後
、取り出すことが望ましい。120℃以上に加熱された
液体または粘稠体が急激に常圧下に排出されて膨張する
ことを防ぐためである。冷却には通常100〜300秒
必要とする。As shown in FIG. 1, it is desirable that the object to be sterilized (1) heated and sterilized in the holding section (7) is taken out after passing through the cooling section (8). This is to prevent liquid or viscous material heated to 120° C. or higher from being suddenly discharged to normal pressure and expanding. Cooling usually requires 100 to 300 seconds.
(実施例)
各種固形物と第1図の装置を使用し、液体の粘度に応じ
て固形物の滞留損失率を測定した。(Example) Using various solids and the apparatus shown in FIG. 1, the retention loss rate of the solids was measured according to the viscosity of the liquid.
パイプ中を移送した時間はおよそ8分であり(予備加熱
180秒、マイクロ波加熱60秒、ホールド60秒、冷
却180秒)、何れも液体及び固形物が均−且つ十分に
殺菌されていた。The time it took to transfer through the pipe was approximately 8 minutes (180 seconds of preheating, 60 seconds of microwave heating, 60 seconds of holding, and 180 seconds of cooling), and the liquid and solids were uniformly and sufficiently sterilized in all cases.
固形物 実施例1 径約10mmのコーン実施例2
径約10 m、mのグリーンピース
実施例3 10mm角のキャロット
実施例4 15mm角の角切牛肉
実施例5 10mm角の角切牛肉
滞留損失率の結果を第2図に示す。なお、滞留損失率と
は(投入した固形物重置−排出した固形物重量)/(投
入した固形物重置)で表される数値であり、いずれの固
形物の結果もNWAで示す範囲に含まれた。Solid material Example 1 Cone example 2 with a diameter of approximately 10 mm
Green peas with a diameter of about 10 m, Example 3 of m green peas Example 4 of 10 mm square carrots Example 5 of 15 mm square cut beef cubes The results of retention loss rate of 10 mm square beef cubes are shown in FIG. In addition, the retention loss rate is a value expressed as (weight of solids input - weight of solids discharged) / (weight of solids input), and the results for both solids are within the range shown by NWA. Included.
(効果)
以上のように、本発明によれば、固形物と液体から成る
混合物を、固形物を沈降することなくパイプ中を移送し
て均一に加熱殺菌することが可能となる。(Effects) As described above, according to the present invention, it is possible to uniformly heat and sterilize a mixture of solids and liquid by transferring it through a pipe without sedimentation of the solids.
第1図は本発明に係る装置を示す説明図、第2図は実施
例における滞留損失率を示すグラフ。
(1) −一−−被殺菌物 (2) −ホッパー(
3)−・・・ポンプ (4)−・−・−パイプ
(5) −−−−一子備加熱装置
(6、)−m−・マイクロ波加熱装置FIG. 1 is an explanatory diagram showing the apparatus according to the present invention, and FIG. 2 is a graph showing the retention loss rate in the example. (1) -1--Object to be sterilized (2) -Hopper (
3) --- Pump (4) --- Pipe (5) --- One-piece heating device (6,) --- Microwave heating device
Claims (1)
をパイプ中を連続的に移送しながら、パイプ周囲に順次
設けられたマイクロ波加熱装置及び断熱状態のホールデ
ィング部により加熱殺菌する加熱殺菌方法において、液
体が粘度2000cp以上であることを特徴とする加熱
殺菌方法。(1) Heating to sterilize objects consisting of solids and liquids with a diameter of 5 to 20 mm while continuously transferring them through the pipe using a microwave heating device and an adiabatic holding section installed around the pipe. A heat sterilization method characterized in that the liquid has a viscosity of 2000 cp or more.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31377190A JP3160903B2 (en) | 1990-11-19 | 1990-11-19 | Heat sterilization method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP31377190A JP3160903B2 (en) | 1990-11-19 | 1990-11-19 | Heat sterilization method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH04183376A true JPH04183376A (en) | 1992-06-30 |
JP3160903B2 JP3160903B2 (en) | 2001-04-25 |
Family
ID=18045329
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP31377190A Expired - Fee Related JP3160903B2 (en) | 1990-11-19 | 1990-11-19 | Heat sterilization method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3160903B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008541706A (en) * | 2005-05-23 | 2008-11-27 | フラウンホッファー−ゲゼルシャフト ツァ フェルダールング デァ アンゲヴァンテン フォアシュンク エー.ファオ | Homogeneous heating method for products |
-
1990
- 1990-11-19 JP JP31377190A patent/JP3160903B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008541706A (en) * | 2005-05-23 | 2008-11-27 | フラウンホッファー−ゲゼルシャフト ツァ フェルダールング デァ アンゲヴァンテン フォアシュンク エー.ファオ | Homogeneous heating method for products |
Also Published As
Publication number | Publication date |
---|---|
JP3160903B2 (en) | 2001-04-25 |
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Legal Events
Date | Code | Title | Description |
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LAPS | Cancellation because of no payment of annual fees |