JPH02261342A - Fluid continuous thermal sterilizer - Google Patents

Fluid continuous thermal sterilizer

Info

Publication number
JPH02261342A
JPH02261342A JP8212289A JP8212289A JPH02261342A JP H02261342 A JPH02261342 A JP H02261342A JP 8212289 A JP8212289 A JP 8212289A JP 8212289 A JP8212289 A JP 8212289A JP H02261342 A JPH02261342 A JP H02261342A
Authority
JP
Japan
Prior art keywords
fluid
hot water
time
sterilization
pipes
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
Application number
JP8212289A
Other languages
Japanese (ja)
Other versions
JP2813678B2 (en
Inventor
Hiromasa Yanase
柳瀬 浩雅
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hisaka Works Ltd
Original Assignee
Hisaka Works Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hisaka Works Ltd filed Critical Hisaka Works Ltd
Priority to JP8212289A priority Critical patent/JP2813678B2/en
Publication of JPH02261342A publication Critical patent/JPH02261342A/en
Application granted granted Critical
Publication of JP2813678B2 publication Critical patent/JP2813678B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To treat many kinds of fluids without waste by providing a device for calculating a discharging time of residual hot water and discharging time of the residual fluid varying with construction of a sterilizing passage and the king of the fluid to be treated. CONSTITUTION:A thermal sterilizer is additionally equipped with a device for inputting data on the number of pipes, connecting pipes, the flow rate, viscosity, etc., of a fluid to be treated of a heater 1, a cooler 3 and other holding pipes 2, etc., composing a sterilizing passage and performing calculation is provided. The purging time of the residual fluid with hot water and purging time of the residual hot water with the fluid are calculated to set the minimum required time.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は牛乳やスープその他の流体の連続加熱殺菌装置
に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a continuous heat sterilization device for milk, soup and other fluids.

従来の技術 従来、この柚の流体連続加熱殺菌装置において、殺菌系
路の熱水による殺菌後の残留熱水を被処理流体によって
追い出す時間並びに流体の殺菌処理後の残留流体の熱水
による追い出し時間は、それぞれ流体の種類によって個
別的に選定し、手動で処理時間を設定していた。
Conventional technology Conventionally, in this continuous heat sterilization apparatus for yuzu fluid, the time required to drive out residual hot water after sterilization with hot water in the sterilization system path by the fluid to be treated, and the time to drive out the residual fluid with hot water after sterilization of the fluid Each was selected individually depending on the type of fluid, and the processing time was manually set.

発明が解法しようとする課題 しかし、上記のように流体の種類による個別的な設定で
は殺菌系路の構成としての配管の太さや長さにより処理
時間が異なる他、流体の処理量や粘度による時間差があ
って、処理時間の割り出しには相当な熟練を要する。そ
して、殺菌処理前の被処理流体による残留熱水の追い出
し時間並びに殺菌処理後に行なわれる熱水による残留流
体の追い出し時間は経験に基づく時間設定をしても安全
性の観点から長くするのが通例であって時間的ロスの他
、流体の無駄も見られ、他品種の流体を同一系路で処理
するには極めて煩雑となる難点が見られた。
Problems to be Solved by the Invention However, as mentioned above, with individual settings depending on the type of fluid, the processing time varies depending on the thickness and length of the piping that constitutes the sterilization system path, and there is also a time difference due to the processing amount and viscosity of the fluid. Therefore, determining the processing time requires considerable skill. Even if the time required to drive out the residual hot water by the fluid to be treated before sterilization treatment and the time to drive out the residual fluid by hot water after sterilization treatment are set based on experience, it is customary to make them longer from a safety perspective. In addition to time loss, there was also waste of fluid, and it was extremely complicated to process fluids of different types through the same system.

本発明の目的は連続した2重チューブ管を有する流体連
続加熱殺菌装置において、殺菌系路の構成と被処理流体
の品種によって異なる残留熱水の追い出し時間と残留流
体の追い出し時間とをあらかじめ演算する装置を設けて
自動制御することにより、多品種の流体処理が無駄なく
行なわれる流体連続加熱殺菌装置を提供しようとするも
のである。
An object of the present invention is to calculate in advance the residual hot water expulsion time and the residual fluid expulsion time, which differ depending on the configuration of the sterilization system path and the type of fluid to be treated, in a fluid continuous heat sterilization device having continuous double tubes. The present invention aims to provide a fluid continuous heat sterilization device that can process a wide variety of fluids without waste by providing a device and automatically controlling the device.

課題を解決するための手段 本発明は上記目的を達成するため、連続した2重チュー
ブ管を有する流体連続加熱殺菌装置において、殺菌系路
を構成する加熱器、冷却器その他ホールドパイプ等の管
本数、連結管及び流体の処理流量と粘度等のデータを入
力して演算する装置を付設し、この装置により前記殺菌
系路の減菌に用いた熱水の残量を被処理流体の導入によ
って追い出す時間と、同殺菌系路による被処理流体の処
理後、流体の残量を熱水によって追い出す時間とをあら
かじめ演算し、最少必要時間を割出して制御信号を出す
制御装置を設けたものである。
Means for Solving the Problems In order to achieve the above object, the present invention provides a fluid continuous heat sterilizer having continuous double tubes, in which the number of tubes such as heaters, coolers and other hold pipes constituting the sterilization system path is reduced. , a connecting pipe and a device that inputs and calculates data such as processing flow rate and viscosity of the fluid are attached, and by this device, the remaining amount of hot water used for sterilizing the sterilization system path is expelled by introducing the fluid to be treated. It is equipped with a control device that calculates in advance the time and the time required to drive out the remaining amount of fluid with hot water after processing the fluid to be treated through the sterilization system, determines the minimum required time, and issues a control signal. .

作用 連続した2重チューブ管を有するので、管1本当りの長
さと本数によって殺菌系路の長さの設定、変更が容易に
行なわれ、熱水及び被処理流体の比重、粘度、処理量に
より殺菌系路を通過する流速が演算でき、熱水による残
留流体の追い出し時間並びに流体による残留熱水の追い
出し時間が割出しできる。従って、この演算結果による
処理時間に従って殺菌系路の駆動時間を制御することに
より必要最少時間の自動設定と流体変化による多品質へ
の対応が可能となる。
Since it has continuous double tubes, the length of the sterilization system can be easily set and changed depending on the length and number of tubes, and the length of the sterilization system can be easily changed depending on the specific gravity, viscosity, and processing amount of the hot water and fluid to be treated. The flow velocity passing through the sterilization system path can be calculated, and the time required to expel the residual fluid by the hot water and the time required to expel the residual hot water by the fluid can be determined. Therefore, by controlling the drive time of the sterilization system in accordance with the processing time based on the calculation result, it is possible to automatically set the required minimum time and to respond to various quality changes due to fluid changes.

実施例 以下、図面に示した実施例を説明する。Example The embodiments shown in the drawings will be described below.

第1図は実施例1を示す。FIG. 1 shows Example 1.

(カッオニキスの場合) 加熱器l・・・21本 ホールドパイプ2・−7本   パターンA冷却器3−
25本 殺菌温度 125℃ γ夜流量   300 I2/ h 流体 (高粘度) 第2図は実施例2を示す。
(In the case of Black Onyx) Heater 1...21 Hold pipes 2-7 Pattern A cooler 3-
25 bottles Sterilization temperature: 125°C γ night flow rate: 300 I2/h Fluid (high viscosity) FIG. 2 shows Example 2.

(ヂキンエキスの場合) 加熱器4・・・+5本 ホールドパイプ5・・・3本   パターンB冷却器6
・・・17本 殺菌温度 130℃ 液流1ffl  400fi/h 流体 (中粘度) 第3図に示した例は実施例3としての殺菌系路であり、
一般式 1)熱水が加熱器から分岐点を経て循環する糸路(連結
管の長さ25.44m)の流過時間(LL)2)熱水が
分岐点よりホールドパイプ冷却器を経る糸路(連結管の
長さ3.80m及び6m)流過時間(し、) 3)液体が分岐点よ、リホールドパイプ、冷却器を経る
糸路(連結管の長さ4.6m、3.80m及び6m)流
過時間(L、) で管内の通過時間が計算できる。
(For Jikin extract) Heater 4...+5 Hold pipes 5...3 Pattern B cooler 6
...17 sterilization temperature 130℃ Liquid flow 1ffl 400fi/h Fluid (medium viscosity) The example shown in Figure 3 is the sterilization system line as Example 3,
General formula 1) Flow time (LL) of the thread path (connecting pipe length 25.44 m) in which hot water circulates from the heater through the branch point 2) Thread in which hot water circulates from the branch point to the hold pipe cooler (Length of connecting pipe: 3.80 m and 6 m) Flow time (shi,) 3) Thread path where liquid passes through the branch point, rehold pipe, and cooler (Length of connecting pipe: 4.6 m, 3. 80m and 6m) The passage time in the pipe can be calculated using the flow time (L, ).

但し、m=管の長さ(2,24m) は管内の流速を示す。However, m = length of pipe (2.24m) indicates the flow velocity in the pipe.

流jM =・X (β/h) ホールドパイプ(管本数)・・・W 加熱器(管本数)・・・y 冷却器(管本数)・−z  とすると 4)液体による分岐点からの循環路(20,84m)の
熱水の追い出し時間(L4) 上記し、 +1.+1.−+−上イが殺菌系路における
熱水及び流体の追い出し時間となる。
Flow jM =・X (β/h) Hold pipe (number of pipes)...W Heater (number of pipes)...y Cooler (number of pipes)・-z 4) Circulation by liquid from branch point Discharge time (L4) of hot water from road (20,84m) As above, +1. +1. -+- A is the time for expelling hot water and fluid in the sterilization system path.

パターンA及びパターン已についても、それぞれ連結管
の長さ、循環路の長さが決定されると計算される。なお
、パターンAB共に加熱器、冷却器及びホールドパイプ
の長さはそれぞれ一本の管の長さを一定として、これら
の本数を掛けることにより容易に演算できる。又パター
ンの変化もこれら管の組合わせにより多品種の流体の加
熱殺菌に応用できる。
For pattern A and pattern length, calculations are also performed once the length of the connecting pipe and the length of the circulation path are determined, respectively. In addition, the lengths of the heater, cooler, and hold pipe for both patterns AB can be easily calculated by multiplying the number of these by assuming that the length of each pipe is constant. Also, by changing the pattern and combining these tubes, it can be applied to heat sterilization of various types of fluids.

発明の効果 本発明は上記のように殺菌系路を構成する管の本数によ
って糸路の設定及び変化に応じることができるので多品
種の流体を利用しても、これら管本数を設定し、流体の
処理流量と粘度等のデータ入力により、容易に系路内の
殺菌に要する熱水の追い出し時間並びに流体の追い出し
時間が演算され、これら演算結果による制御装置の操作
によって加熱殺菌に必要な糸路の確保ができるようにな
った。従って、無駄な時間、流体、熱水を減少し、流体
についても多品種の利用を速刻且つ自動的に設定できる
等その効果は大きい。
Effects of the Invention As described above, the present invention can respond to the setting and change of the thread path depending on the number of pipes constituting the sterilization system path, so even when using a wide variety of fluids, the number of pipes can be set and the By inputting data such as processing flow rate and viscosity, it is easy to calculate the hot water expulsion time and fluid expulsion time required for sterilization in the system, and by operating the control device based on these calculation results, the yarn path necessary for heat sterilization is calculated. It is now possible to secure Therefore, the effects are great, such as reducing wasted time, fluids, and hot water, and making it possible to quickly and automatically set the use of a wide variety of fluids.

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

第1図は加熱器、冷却器、ホールドパイプの接続による
殺菌系路の例を示す斜視図、第2図は他実施例を示す斜
視図、第3図は実際の殺菌系路の説明図である。 1.4.7・・・加熱器 2.5.8・・・ホールドパイプ
Fig. 1 is a perspective view showing an example of a sterilization system route by connecting a heater, a cooler, and a hold pipe, Fig. 2 is a perspective view showing another embodiment, and Fig. 3 is an explanatory diagram of an actual sterilization system route. be. 1.4.7... Heater 2.5.8... Hold pipe

Claims (1)

【特許請求の範囲】[Claims] 連続した2重チューブ管を有する流体連続加熱殺菌装置
において、殺菌系路を構成する加熱器、冷却器その他ホ
ールドパイプ等の管本数、連結管及び流体の処理流量と
粘度等のデータを入力して演算する装置を付設し、この
装置により前記殺菌系路の減菌に用いた熱水の残量を被
処理流体の導入によって追い出す時間と、同殺菌系路に
よる被処理流体の処理後、流体の残量を熱水によって追
い出す時間とをあらかじめ演算し、最少必要時間を割出
して制御信号を出す制御装置を設けたことを特徴とする
流体連続加熱殺菌装置。
In a fluid continuous heat sterilizer that has continuous double tubes, enter data such as the number of pipes such as heaters, coolers, and other hold pipes that make up the sterilization system, connecting pipes, and the processing flow rate and viscosity of the fluid. A device is attached to calculate the time required to expel the remaining amount of hot water used for sterilization in the sterilization system by introducing the fluid to be treated, and the amount of fluid remaining after the fluid to be treated is processed by the sterilization system. 1. A fluid continuous heat sterilization device characterized by being provided with a control device that calculates in advance the time required to expel the remaining amount with hot water, determines the minimum required time, and issues a control signal.
JP8212289A 1989-03-31 1989-03-31 Fluid continuous heating sterilizer Expired - Fee Related JP2813678B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8212289A JP2813678B2 (en) 1989-03-31 1989-03-31 Fluid continuous heating sterilizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8212289A JP2813678B2 (en) 1989-03-31 1989-03-31 Fluid continuous heating sterilizer

Publications (2)

Publication Number Publication Date
JPH02261342A true JPH02261342A (en) 1990-10-24
JP2813678B2 JP2813678B2 (en) 1998-10-22

Family

ID=13765609

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8212289A Expired - Fee Related JP2813678B2 (en) 1989-03-31 1989-03-31 Fluid continuous heating sterilizer

Country Status (1)

Country Link
JP (1) JP2813678B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102437738B1 (en) * 2020-10-27 2022-08-30 (주)마나에프앤비 Various beverage sterilizers that vary the heating time and length of the heating pipe according to the characteristics of the beverage

Also Published As

Publication number Publication date
JP2813678B2 (en) 1998-10-22

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