JPH046554Y2 - - Google Patents

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Publication number
JPH046554Y2
JPH046554Y2 JP12557484U JP12557484U JPH046554Y2 JP H046554 Y2 JPH046554 Y2 JP H046554Y2 JP 12557484 U JP12557484 U JP 12557484U JP 12557484 U JP12557484 U JP 12557484U JP H046554 Y2 JPH046554 Y2 JP H046554Y2
Authority
JP
Japan
Prior art keywords
tank
water
inlet
take
cleaning tank
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
JP12557484U
Other languages
Japanese (ja)
Other versions
JPS6140891U (en
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 filed Critical
Priority to JP12557484U priority Critical patent/JPS6140891U/en
Publication of JPS6140891U publication Critical patent/JPS6140891U/en
Application granted granted Critical
Publication of JPH046554Y2 publication Critical patent/JPH046554Y2/ja
Granted legal-status Critical Current

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  • Apparatuses For Bulk Treatment Of Fruits And Vegetables And Apparatuses For Preparing Feeds (AREA)

Description

【考案の詳細な説明】 〔産業上の利用分野〕 本考案は野菜あるいは漬物等の野菜加工品の殺
菌に用いられる殺菌装置に関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a sterilizer used for sterilizing vegetables or processed vegetable products such as pickles.

〔従来の技術〕[Conventional technology]

従来例を第3図に示す。図において1は殺菌槽
であり内部には空気吹込み管11を備え、出口部
13から入口部12にはポンプ15および加熱手
段17の介在する還流路14が連絡し出口部13
付近には取出しコンベアー16が配置されてい
る。2は洗浄槽であり内部には空気吹込み管21
を備え、入口部22付近には殺菌槽1の取出しコ
ンベアー16が臨出し、出口部23付近には取出
しコンベアー26が配置されている。上記構成に
おいて、殺菌槽1に例えば次亜鉛素酸ソーダーの
ような殺菌剤を含んだ水を満たし、50〜65℃程度
に加温し、かつ空気吹込み管11から該水中に空
気を吹込みつゝ野菜あるいは漬物等の被処理物T
を入口部12から投入する。槽内の水はポンプ1
5により槽1入口部12より出口部13へ流動
し、更に還流路14から槽1入口部12に還流す
る。被処理物Tは槽内で上記殺菌剤を含んだ水に
接触して殺菌されつゝ水流にのつて出口部13に
達し取出しコンベアー16によつて取出され、次
いで洗浄槽2の入口部22に投入されて洗浄槽2
中の水により空気吹込み管21から空気を吹込み
つゝ洗浄されて付着した殺菌剤を除去されるとと
もに冷却され、出口部23に達して取出しコンベ
アー26から取出される。
A conventional example is shown in FIG. In the figure, reference numeral 1 denotes a sterilization tank, which is equipped with an air blowing pipe 11 inside, and a reflux path 14 in which a pump 15 and a heating means 17 are interposed communicates from an outlet section 13 to an inlet section 12.
A take-out conveyor 16 is arranged nearby. 2 is a cleaning tank with an air blowing pipe 21 inside.
A take-out conveyor 16 of the sterilizing tank 1 emerges near the inlet portion 22, and a take-out conveyor 26 is arranged near the outlet portion 23. In the above configuration, the sterilizing tank 1 is filled with water containing a sterilizing agent such as sodium hypozinc oxide, heated to about 50 to 65°C, and air is blown into the water from the air blowing pipe 11. Items to be processed such as vegetables or pickles T
is introduced from the inlet section 12. Water in the tank is pumped 1
5, the water flows from the tank 1 inlet 12 to the outlet 13, and further refluxes from the reflux path 14 to the tank 1 inlet 12. The material to be treated T is sterilized by coming into contact with the water containing the disinfectant in the tank, reaches the outlet section 13 along the water flow, is taken out by the take-out conveyor 16, and is then transferred to the inlet section 22 of the cleaning tank 2. Washing tank 2
The water inside blows air through the air blowing pipe 21 and washes it to remove the attached sterilizer and cools it, and then it reaches the outlet section 23 and is taken out from the take-out conveyor 26.

〔考案が解決しようとする問題点〕[Problem that the invention attempts to solve]

上記従来技術にあつては殺菌槽では被処理物が
加熱され、洗浄槽では冷却される。即ち殺菌槽で
はエネルギーの供給、洗浄槽ではエネルギーの奪
取が行われる。したがつて殺菌槽を独立して加熱
することはエネルギーの有効利用に反するもので
ある。
In the above conventional technology, the object to be treated is heated in the sterilization tank and cooled in the cleaning tank. That is, energy is supplied in the sterilization tank, and energy is taken away in the cleaning tank. Therefore, heating the sterilization tank independently is contrary to the efficient use of energy.

〔問題点を解決するための手段〕[Means for solving problems]

本考案は上記従来の問題点を解決することを目
的とし、上記目的達成のために本考案は前段に殺
菌槽を配し、後段に洗浄手段を配し、該殺菌槽に
はヒートポンプの加熱機構を装着し、該洗浄手段
には該ヒートポンプの冷却機構を装着した構成を
有するものである。
The purpose of the present invention is to solve the above-mentioned conventional problems.To achieve the above-mentioned purpose, the present invention provides a sterilization tank at the front stage, a cleaning means at the rear stage, and a heat pump heating mechanism in the sterilization tank. The cleaning means is equipped with a cooling mechanism for the heat pump.

〔作用〕[Effect]

本考案は上記構成にもとづき、洗浄手段におい
てはヒートポンプの冷却機構によつてエネルギー
を奪取することによつて冷却し、殺菌槽において
は該エネルギーを加熱機構によつて供給して加熱
を行なう。
The present invention is based on the above-mentioned structure, and the cleaning means uses a cooling mechanism of a heat pump to extract energy for cooling, and the sterilizing tank is heated by supplying the energy to a heating mechanism.

〔考案の効果〕[Effect of idea]

本考案は上記構成、作用を有するから洗浄手段
での冷却によつて奪取したエネルギーを殺菌槽の
加熱に利用出来、エネルギー効率が大巾に向上す
る。
Since the present invention has the above-mentioned structure and function, the energy taken by the cooling by the cleaning means can be used for heating the sterilization tank, and the energy efficiency is greatly improved.

〔実施例〕〔Example〕

本考案を第1図に示す一実施例により以下に詳
細に説明すれば、第1図において1は殺菌槽であ
り内部には空気吹込み管11を備え、出口部13
から入口部12にはポンプ15、加熱装置17の
介在する還流路14が連絡し出口部13付近には
取出しコンベアー16が配置されている。取出し
コンベアー16はネツトのような多孔体からなり
上方にはシヤワー3が設置される。2は洗浄槽で
あり内部には空気吹込み管21を備え、入口部2
2付近には殺菌槽1の取出しコンベアー16が臨
出し、出口部23付近には取出しコンベアー26
が配置されている。取出しコンベアー26はコン
ベアー16と同様にネツトのような多孔体からな
り上方にはシヤワー4が設置される。更に洗浄槽
2の出口部23から入口部22にはポンプ25、
冷却装置27の介在する還流路24が連絡する。
そして該洗浄槽2からシヤワー4にポンプ31の
介在する水供給路32が連絡する。
The present invention will be described in detail below with reference to an embodiment shown in FIG. 1. In FIG.
A reflux path 14 in which a pump 15 and a heating device 17 are interposed communicates with the inlet portion 12, and a take-out conveyor 16 is arranged near the outlet portion 13. The take-out conveyor 16 is made of a porous material such as a net, and a shower 3 is installed above it. Reference numeral 2 denotes a cleaning tank, which is equipped with an air blowing pipe 21 inside, and has an inlet section 2.
The take-out conveyor 16 of the sterilization tank 1 emerges near 2, and the take-out conveyor 26 appears near the outlet 23.
is located. Like the conveyor 16, the take-out conveyor 26 is made of a porous material such as a net, and the shower 4 is installed above it. Furthermore, a pump 25 is provided from the outlet section 23 to the inlet section 22 of the cleaning tank 2.
A reflux path 24 with a cooling device 27 is in communication.
A water supply path 32 in which a pump 31 is interposed connects the cleaning tank 2 to the shower 4.

上記加熱装置17の加熱機構52と冷却装置2
7の冷却機構53との間にはヒートポンプシステ
ムHPが適用される。第2図において51はフレ
オン、アンモニア等の媒体を内蔵する閉回路であ
り、該閉回路51には加熱装置17の加熱機構5
2および冷却装置27の冷却機構53が存在し、
更に圧縮機54、乾燥器55、受け器56が介在
し、更に冷却機構53の入口側には膨張弁57、
出口側には吸入圧力調節弁58が介在し、また乾
燥器55と膨張弁57との間には電磁弁59と監
視のためのサイトグラス60が介在し、乾燥器5
5と受け器56との間にはバルブ61が介在して
いる。該閉回路51からは更に補助冷却回路62
が分岐され、該補助冷却回路62には補助凝縮器
63、該補助凝縮器63に送風するフアン64、
凝縮圧力調節弁65が介在し、該フアン64は閉
回路51内の温度を検出するサーモスタツト66
によつて作動される。なお、上記補助凝縮器63
に水冷式のものを用いてもよい。
The heating mechanism 52 of the heating device 17 and the cooling device 2
A heat pump system HP is applied between the cooling mechanism 53 of No. 7 and the cooling mechanism 53 of No. 7. In FIG. 2, 51 is a closed circuit containing a medium such as freon or ammonia, and the heating mechanism 5 of the heating device 17 is connected to the closed circuit 51.
2 and a cooling mechanism 53 of the cooling device 27,
Furthermore, a compressor 54, a dryer 55, and a receiver 56 are interposed, and an expansion valve 57 and an expansion valve 57 are provided on the inlet side of the cooling mechanism 53.
A suction pressure regulating valve 58 is interposed on the outlet side, and a solenoid valve 59 and a sight glass 60 for monitoring are interposed between the dryer 55 and the expansion valve 57.
A valve 61 is interposed between 5 and the receiver 56. An auxiliary cooling circuit 62 is further connected to the closed circuit 51.
The auxiliary cooling circuit 62 includes an auxiliary condenser 63, a fan 64 for blowing air to the auxiliary condenser 63,
A condensing pressure regulating valve 65 is interposed, and the fan 64 is connected to a thermostat 66 that detects the temperature within the closed circuit 51.
operated by. Note that the auxiliary condenser 63
A water-cooled type may also be used.

上記構成において殺菌槽1に例えば次亜鉛素酸
ソーダー、酢酸のような殺菌剤を含んだ水を満た
し50〜80℃程度に加温し、空気吹込み管11から
該水中に空気を吹込みつつ野菜、あるいは漬物の
ような野菜加工物を被処理物Tとして殺菌槽1の
入口部12から投入する。このような処理の際槽
内の水はポンプ15により殺菌槽1入口部12よ
り出口部13へ流動し、更に還流路14から殺菌
槽1入口部12に還流し、この間に水は加熱装置
17により上記温度範囲に加熱せられる。被処理
物Tは槽内で上記殺菌剤を含んだ水に接触して殺
菌されつつ水流にのつて出口部13に達し取出し
コンベアー16によつて取出される。そしてコン
ベアー16上でシヤワー3によつて洗浄槽2から
ポンプ31によつて水供給路32を介しての冷水
を撤布され被処理物Tに付着している殺菌剤を洗
い落す。その後被処理物Tはコンベアー16から
洗浄槽2の入口部22に投入される。洗浄槽2に
おいては洗浄槽2内の水に空気吹込み管21から
空気を吹込みつつ被処理物Tの洗浄を行なう。洗
浄槽2内の水はポンプ25によつて洗浄槽2入口
部22より出口部23へ流動し、更に還流路24
から洗浄槽2入口部22に還流し、この間に水は
冷却装置27により冷却せられる。かくして完全
に殺菌剤を除去された被処理物Tは水流にのつて
洗浄槽2の出口部23に達して取出しコンベアー
26から取出され、シヤワー4によつて水を撤布
されて完全に洗浄される。
In the above configuration, the sterilizing tank 1 is filled with water containing a sterilizing agent such as sodium hypozinc oxide or acetic acid, heated to about 50 to 80°C, and air is blown into the water from the air blowing pipe 11. Vegetables or processed vegetable products such as pickles are fed into the sterilization tank 1 from the inlet 12 as the processed material T. During such treatment, the water in the tank flows from the inlet 12 of the sterilizing tank 1 to the outlet 13 by the pump 15, and then returns to the inlet 12 of the sterilizing tank 1 from the reflux path 14. During this time, the water flows through the heating device 17. is heated to the above temperature range. The material to be treated T comes into contact with water containing the disinfectant in the tank and is sterilized while being carried by the water flow to the outlet section 13 where it is taken out by the take-out conveyor 16. Then, on the conveyor 16, cold water is removed from the cleaning tank 2 by the shower 3 via the water supply path 32 by the pump 31, and the disinfectant adhering to the object T to be treated is washed off. Thereafter, the object to be treated T is introduced from the conveyor 16 into the inlet portion 22 of the cleaning tank 2 . In the cleaning tank 2, the workpiece T is cleaned while blowing air into the water in the cleaning tank 2 from an air blowing pipe 21. The water in the cleaning tank 2 flows from the inlet part 22 of the cleaning tank 2 to the outlet part 23 by the pump 25, and further flows through the reflux path 24.
The water flows back to the inlet section 22 of the cleaning tank 2, and during this period, the water is cooled by the cooling device 27. The object T from which the sterilizer has been completely removed is carried by the water flow to the outlet 23 of the washing tank 2 and taken out from the take-out conveyor 26, where the water is removed by the shower 4 and the object T is completely washed. Ru.

ヒートポンプシステムHPにおいて閉回路51
を循環する媒体は圧縮機54によつて圧縮液化さ
れ、加熱装置17の加熱機構52で放熱すること
によつて加熱装置17を加熱し、放熱した媒体は
受け器56に備蓄され、バルブ61を介して乾燥
器55によつて除湿された後冷却装置27の冷却
機構53で気化して洗浄槽2からの水を冷却す
る。このようにして気化した媒体は吸入圧力調節
弁58によつて吸入圧力を所定に調節されて、再
び圧縮機54に循環する。上記ヒートポンプシス
テムHPにおいて圧縮機54の機械的仕事量にも
とづく熱量が余分に媒体に加わり系内の媒体温度
は次第に上昇し、圧力も上昇する。所定の圧力上
昇に達すれば、凝縮圧力調整弁65が開き、媒体
が補助凝縮器63を流れ、周囲に放熱することに
よりヒートバランスをとる。更に、周囲温度が高
いとか通風が悪いとかの放熱条件が悪いときは、
サーモスタツト66によつてこれを検出しフアン
64を作動させて補助凝縮器63を通過する媒体
を空冷しヒートバランスをとる。
Closed circuit 51 in heat pump system HP
The circulating medium is compressed and liquefied by the compressor 54, and the heating mechanism 52 of the heating device 17 radiates heat to heat the heating device 17. The radiated medium is stored in the receiver 56 and the valve 61 is heated. The water from the cleaning tank 2 is cooled by being dehumidified by the dryer 55 and vaporized by the cooling mechanism 53 of the cooling device 27 . The suction pressure of the thus vaporized medium is adjusted to a predetermined value by the suction pressure regulating valve 58, and the medium is circulated to the compressor 54 again. In the heat pump system HP, an extra amount of heat is added to the medium based on the mechanical work of the compressor 54, and the temperature of the medium in the system gradually rises, and the pressure also rises. When a predetermined pressure rise is reached, the condensing pressure regulating valve 65 opens, the medium flows through the auxiliary condenser 63, and heat balance is achieved by radiating heat to the surroundings. Furthermore, if heat dissipation conditions are poor, such as high ambient temperature or poor ventilation,
This is detected by the thermostat 66 and the fan 64 is operated to air-cool the medium passing through the auxiliary condenser 63 to achieve heat balance.

本実施例以外殺菌槽の後段の洗浄手段はシヤワ
ーのみであつても洗浄槽のみであつてもよい。
Other than this embodiment, the cleaning means after the sterilization tank may be only a shower or only a cleaning tank.

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

第1図および第2図は本考案にかかる一実施例
を示し、第1図は殺菌装置の系統図、第2図はヒ
ートポンプシステムの系統図であり、第3図は従
来例の系統図である。 図中、1……殺菌槽、2……洗浄槽、17……
加熱装置、27……冷却装置、52……加熱機
構、53……冷却機構。
Figures 1 and 2 show an embodiment of the present invention, Figure 1 is a system diagram of a sterilizer, Figure 2 is a system diagram of a heat pump system, and Figure 3 is a system diagram of a conventional example. be. In the figure, 1... sterilization tank, 2... cleaning tank, 17...
Heating device, 27... Cooling device, 52... Heating mechanism, 53... Cooling mechanism.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 前段に殺菌槽を配し、後段に洗浄手段を配し、
該殺菌槽にはヒートポンプの加熱機構を装着し、
該洗浄手段にはヒートポンプの冷却機構を装着し
たことを特徴とする野菜の殺菌装置。
A sterilization tank is placed in the front stage, and a cleaning means is placed in the rear stage.
The sterilization tank is equipped with a heat pump heating mechanism,
A vegetable sterilizer characterized in that the cleaning means is equipped with a heat pump cooling mechanism.
JP12557484U 1984-08-17 1984-08-17 vegetable sterilizer Granted JPS6140891U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12557484U JPS6140891U (en) 1984-08-17 1984-08-17 vegetable sterilizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12557484U JPS6140891U (en) 1984-08-17 1984-08-17 vegetable sterilizer

Publications (2)

Publication Number Publication Date
JPS6140891U JPS6140891U (en) 1986-03-15
JPH046554Y2 true JPH046554Y2 (en) 1992-02-21

Family

ID=30684268

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12557484U Granted JPS6140891U (en) 1984-08-17 1984-08-17 vegetable sterilizer

Country Status (1)

Country Link
JP (1) JPS6140891U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018096764A1 (en) * 2016-11-28 2018-05-31 株式会社アドメテック Washing system for agricultural product and washing method for agricultural product

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4609652B2 (en) * 2005-07-26 2011-01-12 井関農機株式会社 Crop cleaning machine
JP2012191910A (en) * 2011-03-17 2012-10-11 Tokyo Electric Power Co Inc:The Sterilization system
JP5510491B2 (en) * 2012-04-23 2014-06-04 井関農機株式会社 Seed disinfection equipment
JP5614444B2 (en) * 2012-12-05 2014-10-29 井関農機株式会社 Hot water treatment equipment

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018096764A1 (en) * 2016-11-28 2018-05-31 株式会社アドメテック Washing system for agricultural product and washing method for agricultural product
JPWO2018096764A1 (en) * 2016-11-28 2019-03-28 株式会社アドメテック Agricultural product cleaning system and agricultural product cleaning method

Also Published As

Publication number Publication date
JPS6140891U (en) 1986-03-15

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