JPH0138467B2 - - Google Patents

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Publication number
JPH0138467B2
JPH0138467B2 JP56150143A JP15014381A JPH0138467B2 JP H0138467 B2 JPH0138467 B2 JP H0138467B2 JP 56150143 A JP56150143 A JP 56150143A JP 15014381 A JP15014381 A JP 15014381A JP H0138467 B2 JPH0138467 B2 JP H0138467B2
Authority
JP
Japan
Prior art keywords
liquid
valve
flow rate
filling machine
automatic
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.)
Expired
Application number
JP56150143A
Other languages
Japanese (ja)
Other versions
JPS5851973A (en
Inventor
Mitsuichi Yoshikawa
Shogo Yamaguchi
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP56150143A priority Critical patent/JPS5851973A/en
Publication of JPS5851973A publication Critical patent/JPS5851973A/en
Publication of JPH0138467B2 publication Critical patent/JPH0138467B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は、飲料等の液を加熱殺菌して充填機へ
送るための液処理装置の改良に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a liquid processing device for heating and sterilizing liquids such as beverages and sending the sterilized liquids to a filling machine.

第1図は従来のものの一例を示す図で、常温の
製品液は製品液供給入口1より、クツシヨンタン
ク2に供給される。製品液は、クツシヨンタンク
2より送液配管3を経て圧送ポンプ4に吸引さ
れ、加圧された製品液は、異物分離器5を経て、
熱交換器6の加熱殺菌部7に流入する。温度指示
調節警報計8は、熱交換器6の加熱殺菌部7より
流出する製品液温度を検出して、その加熱殺菌温
度の制御を行なう。具体的には、熱媒体循環装置
16の制御を行なうと同時に、検出した製品液温
度(殺菌温度)が設定した下限温度未満又は、上
限温度を越えた時は、三方切換弁9の流路を液戻
し配管13側に自動的に切換える。所定の殺菌温
度条件(殺菌温度が下限温度以上及び上限温度以
下の範囲内にある場合)を満足している時、三方
切換弁9は正流側に切換えられており、製品液
は、フイルター10及び第2の三方切換弁11を
経て、充填機送液配管20に至り、充填機に圧送
される。第2の三方切換弁11は、充填機での液
消費がない時又は、充填機側で製品液の供給を必
要としない時、製品液の流路を液戻し側に切換え
て、逆止弁12を経て液戻し配管13側にその流
路を切換るものである。第1の三方切換弁9で戻
し側に切換えられた加熱殺菌温度条件が十分でな
い製品液又は第2の三方切換弁11で戻し側に切
換えられた余剰な製品液は、液戻し配管を経て、
熱交換器6の戻し液冷却部14に流入する。この
戻し液冷却部14では、冷却水供給口17より供
給される冷却水にて所定の温度以下になるように
製品液を冷却し、絞り弁15及びクツシヨンタン
クへの液戻し配管19を経由して、クツシヨンタ
ンク2へ液を戻すようにしている。
FIG. 1 is a diagram showing an example of a conventional type, in which product liquid at room temperature is supplied to a cushion tank 2 from a product liquid supply inlet 1. The product liquid is sucked from the cushion tank 2 through the liquid supply pipe 3 to the pressure pump 4, and the pressurized product liquid passes through the foreign matter separator 5.
It flows into the heat sterilization section 7 of the heat exchanger 6. The temperature indication adjustment alarm meter 8 detects the temperature of the product liquid flowing out from the heat sterilization section 7 of the heat exchanger 6, and controls the heat sterilization temperature. Specifically, at the same time as controlling the heat medium circulation device 16, when the detected product liquid temperature (sterilization temperature) is less than the set lower limit temperature or exceeds the set upper limit temperature, the flow path of the three-way switching valve 9 is closed. Automatically switches to the liquid return piping 13 side. When the predetermined sterilization temperature condition (when the sterilization temperature is within the range of the lower limit temperature or higher and the upper limit temperature or lower), the three-way switching valve 9 is switched to the forward flow side, and the product liquid flows through the filter 10. The liquid then passes through the second three-way switching valve 11, reaches the filling machine liquid sending piping 20, and is fed under pressure to the filling machine. The second three-way switching valve 11 is a check valve that switches the product liquid flow path to the liquid return side when there is no liquid consumption in the filling machine or when there is no need to supply product liquid on the filling machine side. 12, the flow path is switched to the liquid return pipe 13 side. The product liquid switched to the return side by the first three-way switching valve 9 and whose heat sterilization temperature conditions are not sufficient or the excess product liquid switched to the return side by the second three-way switching valve 11 is passed through the liquid return piping,
It flows into the return liquid cooling section 14 of the heat exchanger 6. In this return liquid cooling section 14, the product liquid is cooled to a predetermined temperature or lower using cooling water supplied from a cooling water supply port 17, and is then returned to the liquid through a throttle valve 15 and a liquid return pipe 19 to the cushion tank. Then, the liquid is returned to the cushion tank 2.

しかし、上記した従来のものは、次のような問
題を有している。
However, the conventional device described above has the following problems.

通常の製品生産全運転時間100%に対して、上
述の充填機の運転は、容器の供給又は排出の条件
等々の理由で起動、停止を繰り返しその稼動率は
略々85〜90%である。従つて、製品生産全運転時
間の10〜15%に相当する時間は製品液の流路を液
戻し側に切換えており、その間、加熱の為に加熱
エネルギーを費やすと共に戻し液をほぼ常温迄冷
却する為に冷却水を消費しており、その消費量は
かなりのものであつて、無駄なエネルギー及び資
源の消費により著しく不経済であつた。
While the total operating time for normal product production is 100%, the operation rate of the filling machine described above is approximately 85 to 90% due to repeated startups and stops due to conditions such as supplying or discharging containers. Therefore, during the time equivalent to 10 to 15% of the total product production operation time, the flow path of the product liquid is switched to the liquid return side, and during this time, heating energy is expended for heating and the return liquid is cooled to almost room temperature. This consumes a considerable amount of cooling water and is extremely uneconomical due to wasted energy and resource consumption.

本発明は、上記した点を鑑み提案されたもの
で、その目的とするところは、加熱エネルギーや
冷却水の消費量を大幅に削減することのできる経
済的な液処理装置を提供することにある。
The present invention has been proposed in view of the above points, and its purpose is to provide an economical liquid processing device that can significantly reduce the consumption of heating energy and cooling water. .

本発明は、クツシヨンタンクから圧送ポンプ、
加熱殺菌用熱交換器、殺菌温度が異常のとき、流
路を液戻し側に切換える第1の三方切換自動弁、
充填機での液消費がないとき、流路を液戻し側に
切換える第2の三方切換自動弁を経て充填機へ加
熱殺菌された液を送るようにした液処理装置にお
いて、前記熱交換器の入口側に、前記第1及び第
2の三方切換自動弁の一方が液戻し側に切換つた
とき、及び充填機への送液流量が設定液量以下に
なつたとき、流量を調節する第1の流量調節自動
弁を、また、前記第2の三方切換自動弁の出口側
に、充填機での液消費量に応じた液を送液する第
2の流量調節自動弁を設けると共に前記第1の流
量調節自動弁の入口側に、同弁の開度に応じて液
を戻し側にバイパスさせる流路を設けたことを特
徴とするもので、上記の如く第1及び第2の流量
調節自動弁並びにバイパス流路を設けたことによ
り、充填機での液消費量に応じた液を送液するこ
とができると共に運転中に各機器での異常圧力上
昇を防止することができ、しかも充填機での液消
費量に応じた送液ができるので、無駄な加熱エネ
ルギーを必要とせず、また充填機での液消費量が
設定流量以下になつたり、あるいは充填機が一時
運休したりしたとき等には、熱交換器に入る前に
液を戻し側にバイパスさせることができるので、
加熱エネルギーや冷却水の大幅な削減が可能とな
るため、著しく経済的であり、さらに、無駄な加
熱、冷却することがさけられるので、液の品質劣
化をも防止することができる。
The present invention provides a pressure pump from a cushion tank,
A heat exchanger for heat sterilization, a first three-way automatic switching valve that switches the flow path to the liquid return side when the sterilization temperature is abnormal;
In the liquid processing device, the heat-sterilized liquid is sent to the filling machine via a second three-way automatic switching valve that switches the flow path to the liquid return side when there is no liquid consumption in the filling machine. On the inlet side, a first valve adjusts the flow rate when one of the first and second three-way automatic switching valves switches to the liquid return side and when the flow rate of liquid sent to the filling machine becomes less than the set liquid volume. Further, a second automatic flow rate adjustment valve is provided on the outlet side of the second three-way switching automatic valve for feeding a liquid according to the amount of liquid consumed by the filling machine, and a second automatic flow rate adjustment valve is provided on the outlet side of the second three-way automatic valve. A flow path is provided on the inlet side of the automatic flow rate adjustment valve to bypass the liquid to the return side according to the opening degree of the valve, and as described above, the first and second automatic flow rate adjustment valves are By providing valves and bypass channels, it is possible to send liquid according to the amount of liquid consumed by the filling machine, and it is also possible to prevent abnormal pressure rises in each device during operation. Since the liquid can be fed according to the amount of liquid consumed by the filling machine, there is no need for wasted heating energy, and when the liquid consumption of the filling machine falls below the set flow rate or the filling machine is temporarily suspended, etc. The liquid can be bypassed to the return side before entering the heat exchanger.
It is extremely economical because heating energy and cooling water can be significantly reduced, and wasteful heating and cooling can be avoided, so deterioration of liquid quality can be prevented.

以下、本発明の実施例を第2図に基づいて説明
する。
Hereinafter, embodiments of the present invention will be described based on FIG. 2.

aは未殺菌の製品液供給口、bはクツシヨンタ
ンク、cは送液配管、dは未殺菌の製品液圧送ポ
ンプ、eは異物分離器で、圧送ポンプにて送液さ
れる未殺菌製品液中の固型分等の異物を除去する
ものである。fはバイパス自動弁で、製品液の流
れが第1の流量調節自動弁gにて絞られた時未殺
菌の製品液の一部を自動的にバイパスさせるもの
である。
a is an unsterilized product liquid supply port, b is a cushion tank, c is a liquid delivery pipe, d is an unsterilized product liquid pressure pump, e is a foreign matter separator, and the unsterilized product is sent by the pressure pump. This removes foreign substances such as solids in the liquid. f is an automatic bypass valve that automatically bypasses a portion of the unsterilized product liquid when the flow of the product liquid is throttled by the first automatic flow rate adjustment valve g.

第1の流量調節自動弁gは、充填機での製品液
消費量あるいは運転の状態によつて製品液の流量
を自動的に調節する自動弁で、後述する信号Z2
によつて開閉しその開度が定まる。hは熱交換器
で、未殺菌の製品液を加熱殺菌する加熱殺菌セク
シヨンiと、殺菌不十分な製品液又は充填機から
の戻し液を冷却する戻し液冷却セクシヨンsとか
らなる。jは熱交換器hの加熱殺菌セクシヨンi
で未殺菌の製品液を、加熱殺菌する為に熱を補給
する熱媒体循環装置である。
The first automatic flow rate adjustment valve g is an automatic valve that automatically adjusts the flow rate of the product liquid depending on the consumption amount of the product liquid in the filling machine or the operating state, and receives a signal Z2, which will be described later.
It opens and closes depending on the opening degree. h is a heat exchanger consisting of a heat sterilization section i for heating and sterilizing unsterilized product liquid, and a return liquid cooling section s for cooling insufficiently sterilized product liquid or liquid returned from the filling machine. j is heat sterilization section i of heat exchanger h
This is a heat medium circulation device that supplies heat to heat and sterilize unsterilized product liquid.

kは、製品液の殺菌加熱温度を計測する殺菌温
度指示警報計で、加熱殺菌温度の上・下限を設定
し得るものである。
K is a sterilization temperature indicator and alarm meter that measures the sterilization heating temperature of the product liquid, and is capable of setting the upper and lower limits of the heating sterilization temperature.

1は第1の三方切換自動弁で、殺菌温度指示警
報計kで検出した製品液の殺菌温度が正常(設定
温度範囲内)であれば、その流路を正流側のフイ
ルターm側に切換え、製品液の殺菌温度が異常
(設定温度の下限未満又は上限以上の範囲外)で
あればその流路を戻流側の液戻し配管r側に自動
的に切換る弁である。
1 is the first three-way switching automatic valve, which switches the flow path to the forward flow side of the filter m if the sterilization temperature of the product liquid detected by the sterilization temperature indicator k is normal (within the set temperature range). , is a valve that automatically switches the flow path to the liquid return pipe r side on the return flow side if the sterilization temperature of the product liquid is abnormal (outside the range below the lower limit or above the upper limit of the set temperature).

mは製品液のフイルター、nは第2の三方切換
自動弁で、この第2の三方切換自動弁nは、充填
機での製品液消費がある時、正流側の第2の流量
調節自動弁φ側に切換え、充填機での製品液消費
がない時には、戻流側の逆止弁q側に切換る自動
弁である。
m is a product liquid filter, n is a second three-way switching automatic valve, and this second three-way switching automatic valve n is used to automatically adjust the second flow rate on the forward flow side when the product liquid is consumed in the filling machine. It is an automatic valve that switches to the valve φ side, and switches to the return flow side check valve q side when there is no product liquid consumption in the filling machine.

第2の流量調節自動弁φは、充填機での製品液
消費信号Z1によつて開閉し、その開度が定まる
自動弁で、充填機での製品液消費に応じた製品液
を充填機への送液配管pを通して、充填機に送液
する。第1の三方切換自動弁1又は第2の三方切
換自動弁nにて、液戻し配管r側に切換えられた
製品液は、熱交換器hの戻し液冷却セクシヨンs
にて所定の温度以下に冷却される。
The second flow rate adjustment automatic valve φ is an automatic valve that opens and closes in response to the product liquid consumption signal Z1 in the filling machine, and its opening degree is determined, and supplies the product liquid to the filling machine according to the product liquid consumption in the filling machine. The liquid is sent to the filling machine through the liquid sending pipe p. The product liquid transferred to the liquid return pipe r side by the first three-way automatic switching valve 1 or the second three-way automatic switching valve n is transferred to the return liquid cooling section s of the heat exchanger h.
is cooled down to a predetermined temperature or lower.

tは流量調節弁で戻し液の流量を制限するもの
である。
t is a flow rate control valve that limits the flow rate of the returned liquid.

vは戻し液の冷却水の供給口、wは冷却水供給
自動弁で、第1の三方切換自動弁1は第2の三方
切換自動弁nのいずれかが液戻し配管r側に、そ
の流路が切換えられている時のみに、自動的に全
開となる弁である。
v is a cooling water supply port for the return liquid, w is a cooling water supply automatic valve, and the first three-way switching automatic valve 1 is connected to the liquid return piping r side when either one of the second three-way switching automatic valve n is connected to the This valve automatically opens fully only when the path is switched.

xは、冷却水の流量調節弁で、使用済の冷却水
は流出口yよりドレン又は別装置に流用される。
x is a cooling water flow control valve, and used cooling water is diverted to a drain or another device from an outlet y.

所定の温度以下に冷却された戻し液は、戻し配
管uにてクツシヨンタンクbに戻されるようにな
つている。
The return liquid cooled to a predetermined temperature or lower is returned to the cushion tank b through a return pipe u.

上記の構成において、熱媒体循環装置jは、必
要な熱媒体循環流量を確保し、かつ熱交換器hの
加熱殺菌セクシヨンiに設定した熱媒体供給温度
に制御して、熱媒体を送液循環させる。
In the above configuration, the heat medium circulation device j secures the necessary heat medium circulation flow rate, controls the heat medium supply temperature to the heat sterilization section i of the heat exchanger h, and sends and circulates the heat medium. let

クツシヨンタンクbから圧送ポンプdにより圧
送される未殺菌の製品液は異物分離器e、第1の
流量調節自動弁gを経て、熱交換器hに入り、加
熱殺菌セクシヨンiで加熱殺菌され、第1の三方
切換自動弁1、フイルターm、第2の三方切換自
動弁n、第2の流量調節自動弁φを経て充填機へ
と送液される。
The unsterilized product liquid pumped from the cushion tank b by the pressure pump d passes through the foreign matter separator e and the first automatic flow rate adjustment valve g, enters the heat exchanger h, and is heated and sterilized in the heat sterilization section i. The liquid is sent to the filling machine via the first three-way automatic valve 1, the filter m, the second three-way automatic valve n, and the second flow rate adjustment automatic valve φ.

ここで、第2の流量調節自動弁φは、加熱殺菌
剤製品液を充填機に送液する流量を自動的に調節
するもので、充填機からの製品液消費量に応じた
比例制御信号Z1によつて弁は開閉されその開度
が定まるようになつており、消費量に応じた量の
製品液を送液する。
Here, the second flow rate adjustment automatic valve φ automatically adjusts the flow rate for sending the heated sterilizer product liquid to the filling machine, and uses a proportional control signal Z1 according to the consumption amount of the product liquid from the filling machine. The valve is opened and closed, and its opening degree is determined, and an amount of product liquid is delivered in accordance with the consumption amount.

また、第1の流量調節自動弁gは、その開度を
制御する信号Z2によつてその開度が定まるもの
でありこの制御信号Z2は、第1の三方切換自動
弁1又は第2の三方切換自動弁nのいずれか一方
がその流路を液戻し側、つまり、充填機に送液す
る必要のない条件の時に第1の流量調節自動弁g
の必要開度を与えると同時に、充填機への送液流
量が設定流量よりも少なくなつた時に、熱交換器
h等々の機能品に、圧送ポンプdの吐出圧力が必
要以上にかからないように第1の流量調節自動弁
gの開度を与える。そして、第1の流量調節自動
弁gの開度が絞られると、バイパス自動弁fがそ
れに応じて開き、液をバイパスさせ、第1の流量
調節自動弁gの一次側製品圧力を一定に保つよう
に作用する。これによつて異物分離器eにて液が
滞るのを防止する事、圧送ポンプdの吐出口よ
り、第1の流量調節自動弁gの一次側に至る機能
品が圧送ポンプdの締切圧力によつて異常昇圧し
ないよう防止する事、第1の流量調節自動弁gと
第2の流量調節自動弁φとの連動による製品液の
流量制御をし易くする事ができる。
Further, the opening degree of the first automatic flow rate adjustment valve g is determined by a signal Z2 that controls the opening degree, and this control signal Z2 is used to control the opening degree of the first three-way automatic valve 1 or the second three-way automatic valve g. When one of the automatic switching valves n has its flow path on the liquid return side, that is, when there is no need to send liquid to the filling machine, the first automatic flow rate adjustment valve g
At the same time, when the flow rate of liquid sent to the filling machine becomes lower than the set flow rate, the discharge pressure of the pressure pump d is not applied to functional components such as the heat exchanger h more than necessary. The opening degree of the automatic flow rate adjustment valve g of No. 1 is given. When the opening degree of the first automatic flow rate adjustment valve g is reduced, the automatic bypass valve f opens accordingly, bypassing the liquid, and keeping the primary product pressure of the first automatic flow rate adjustment valve g constant. It works like this. This prevents the liquid from stagnation in the foreign matter separator e, and the functional components from the discharge port of the pressure pump d to the primary side of the first automatic flow control valve g reach the cut-off pressure of the pressure pump d. Therefore, abnormal pressure rise can be prevented, and the flow rate of the product liquid can be easily controlled by interlocking the first automatic flow rate adjustment valve g and the second automatic flow rate adjustment valve φ.

以上の説明から明らかなように、本実施例によ
ると、次のような実用的価値の高い効果を得るこ
とができる。
As is clear from the above description, according to this embodiment, the following effects with high practical value can be obtained.

(1) 充填機での製品液消費量に応じた加熱殺菌済
製品液を、充填機に送液する事が可能である。
(1) It is possible to send heat-sterilized product liquid to the filling machine according to the amount of product liquid consumed by the filling machine.

(2) 運転中に、異物分離器、熱交換器、フイルタ
ー、自動弁類、及び配管等の機能品における異
常圧力上昇を防止し得、それら機能品の耐久性
を保持し得る。
(2) During operation, abnormal pressure increases in functional components such as foreign matter separators, heat exchangers, filters, automatic valves, and piping can be prevented, and the durability of these functional components can be maintained.

(3) 上記(1)の効果により、充填機が製造運転中、
無駄な加熱エネルギーを必要としないと同時
に、従来のものでは、例えば充填機での製品液
消費が半減した時には、その一部を冷却液戻し
をしていたが、本実施例ではその必要がなく、
この場合の冷却水消費を不要にできる。
(3) Due to the effect of (1) above, when the filling machine is in production operation,
At the same time, it does not require wasted heating energy, and in conventional systems, for example, when the product liquid consumption in the filling machine was halved, a part of it was returned to the cooling liquid, but this is not necessary in this embodiment. ,
Cooling water consumption in this case can be made unnecessary.

(4) 充填機が一時運転を休止している時に、従来
のものでは所定の製品液流量(充填機の製品液
消費に見合つた液流量)を熱交換器にて加熱殺
菌し、更にその流路を液戻し側に切換て冷却リ
ターンしていたため、加熱の為のエネルギー
と、冷却の為の冷却水とを浪費していたが、本
実施例では製品液の品質を劣化させる事のない
最低限度、又は製品液の品質劣化が全然問題無
ければ熱交換器への製品液送液を一時停止する
事も可能で、かつその流量が調節可能であるた
め、従来のものと比較して、充填機が一時運転
休止している時の加熱エネルギーと冷却水との
消費を半分以下場合によつては不要とする事が
できる。
(4) When the filling machine is temporarily out of operation, conventional methods heat and sterilize a predetermined product liquid flow rate (liquid flow rate commensurate with the product liquid consumption of the filling machine) using a heat exchanger, and then Since the path was switched to the liquid return side to return the liquid for cooling, energy for heating and cooling water for cooling were wasted. If there is no problem with the limit or quality deterioration of the product liquid, it is possible to temporarily stop feeding the product liquid to the heat exchanger, and the flow rate can be adjusted. The consumption of heating energy and cooling water when the machine is temporarily out of operation can be reduced to less than half, or even become unnecessary in some cases.

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

第1図は従来のものの一例を示す構成図、第2
図は本発明の一実施例を示す構成図である。 b:クツシヨンタンク、d:圧送ポンプ、f:
バイパス自動弁、g:第1の流量調節自動弁、
h:熱交換器、1:第1の三方切換自動弁、n:
第2の三方切換自動弁、φ:第2の流量調節自動
弁、r,u:液戻し配管。
Figure 1 is a configuration diagram showing an example of a conventional one;
The figure is a configuration diagram showing an embodiment of the present invention. b: cushion tank, d: pressure pump, f:
Bypass automatic valve, g: first flow rate adjustment automatic valve,
h: heat exchanger, 1: first three-way automatic valve, n:
Second three-way switching automatic valve, φ: second flow rate adjustment automatic valve, r, u: liquid return piping.

Claims (1)

【特許請求の範囲】[Claims] 1 クツシヨンタンクから圧送ポンプ、加熱殺菌
用熱交換器、殺菌温度が異常のとき、流路を液戻
し側に切換える第1の三方切換自動弁、充填機で
の液消費がないとき、流路を液戻し側に切換える
第2の三方切換自動弁を経て充填機へ加熱殺菌さ
れた液を送るようにした液処理装置において、前
記熱交換器の入口側に、前記第1及び第2の三方
切換自動弁の一方が液戻し側に切換つたとき、及
び充填機への送液流量が設定液量以下になつたと
き、流量を調節する第1の流量調節自動弁を、ま
た、前記第2の三方切換自動弁の出口側に、充填
機での液消費量に応じた液を送液する第2の流量
調節自動弁を設けると共に前記第1の流量調節自
動弁の入口側に、同弁の開度に応じて液を戻し側
にバイパスさせる流路を設けたことを特徴とする
液処理装置。
1. From the cushion tank to the pressure pump, the heat exchanger for heat sterilization, the first three-way automatic valve that switches the flow path to the liquid return side when the sterilization temperature is abnormal, and the flow path when there is no liquid consumption in the filling machine. In the liquid processing apparatus, the heat-sterilized liquid is sent to the filling machine via a second three-way automatic switching valve that switches the liquid to the liquid return side. When one of the automatic switching valves is switched to the liquid return side, and when the flow rate of liquid sent to the filling machine becomes less than the set liquid volume, A second flow rate adjustment automatic valve is provided on the outlet side of the three-way switching automatic valve to send liquid according to the amount of liquid consumed by the filling machine, and a second flow rate adjustment automatic valve is provided on the inlet side of the first flow rate adjustment automatic valve. A liquid processing device characterized in that a flow path is provided for bypassing the liquid to the return side according to the opening degree of the liquid processing device.
JP56150143A 1981-09-22 1981-09-22 Apparatus for treating liquid Granted JPS5851973A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56150143A JPS5851973A (en) 1981-09-22 1981-09-22 Apparatus for treating liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56150143A JPS5851973A (en) 1981-09-22 1981-09-22 Apparatus for treating liquid

Publications (2)

Publication Number Publication Date
JPS5851973A JPS5851973A (en) 1983-03-26
JPH0138467B2 true JPH0138467B2 (en) 1989-08-14

Family

ID=15490427

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56150143A Granted JPS5851973A (en) 1981-09-22 1981-09-22 Apparatus for treating liquid

Country Status (1)

Country Link
JP (1) JPS5851973A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63169896U (en) * 1987-04-27 1988-11-04
JPH04110874U (en) * 1991-03-08 1992-09-25 株式会社ユーシン Transmitter for keyless entry system
JP5271138B2 (en) * 2009-03-30 2013-08-21 サントリー食品インターナショナル株式会社 Recipe for potable water

Also Published As

Publication number Publication date
JPS5851973A (en) 1983-03-26

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