JPS5811984B2 - Sauce circulation concentration dipping equipment for sugar solutions, etc. - Google Patents

Sauce circulation concentration dipping equipment for sugar solutions, etc.

Info

Publication number
JPS5811984B2
JPS5811984B2 JP54117019A JP11701979A JPS5811984B2 JP S5811984 B2 JPS5811984 B2 JP S5811984B2 JP 54117019 A JP54117019 A JP 54117019A JP 11701979 A JP11701979 A JP 11701979A JP S5811984 B2 JPS5811984 B2 JP S5811984B2
Authority
JP
Japan
Prior art keywords
container
dripping liquid
liquid
concentration
dripping
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
JP54117019A
Other languages
Japanese (ja)
Other versions
JPS5642551A (en
Inventor
向井勇
祝出富夫
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 JP54117019A priority Critical patent/JPS5811984B2/en
Publication of JPS5642551A publication Critical patent/JPS5642551A/en
Publication of JPS5811984B2 publication Critical patent/JPS5811984B2/en
Expired legal-status Critical Current

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  • Storage Of Fruits Or Vegetables (AREA)
  • General Preparation And Processing Of Foods (AREA)

Description

【発明の詳細な説明】 本発明は、栗、煮豆、つくだ煮、コンブ又はサクランボ
等の食品原料に糖液、点液又は食品用染料などのたれ液
を均一に且つ短時間に浸透させる、ことができるたれ液
循環濃縮浸漬装置に関するもので、その目的とするとこ
ろは、たれ液濃度調整が容易で、均一化が得られ密閉容
器中で比較的低温で処理でき、極めて生産性が高く、良
品質の加工食品が得られるコンパクトな装置を提供しよ
うとするものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention is capable of uniformly and quickly penetrating a sauce such as a sugar solution, a spot solution, or a food dye into food materials such as chestnuts, boiled beans, tsukudani, kelp, or cherries. This is a dipping device that circulates and concentrates drippings, and its purpose is to easily adjust the concentration of drippings, achieve uniformity, process in a closed container at a relatively low temperature, have extremely high productivity, and produce high quality products. The aim is to provide a compact device that can produce processed foods.

従来一般に、栗等の加工食品を作る装置としては、第3
図に示すように濃度の異なる容器を複数用意し、まず一
番低濃度のたれ液中に食品原料を所定時間浸漬し、次い
でこれより高濃度のたれ液中に所定時間浸漬し、順次こ
れを繰り返すことによって最終目的の加工食品にしてい
る。
Conventionally, the third type of equipment for making processed foods such as chestnuts was generally used.
As shown in the figure, prepare multiple containers with different concentrations, and first immerse the food ingredients in the sauce with the lowest concentration for a predetermined time, then in the sauce with a higher concentration for a predetermined time, and then By repeating the process, it becomes the final processed food.

しかし、これら容器内のたれ液は加工処理をすることに
より食品原料から出て来た水分によって薄まるので、別
途準備されたジャケット式の煮釜で煮沸して、所定濃度
に濃縮して再利用するという工程を採らなければならな
い。
However, as the drippings in these containers are diluted by the moisture released from the food ingredients during processing, they must be boiled in a separately prepared jacket-type boiler, concentrated to a predetermined concentration, and reused. This process must be adopted.

そして、さらにこのような従来法においては次のような
問題点がある。
Furthermore, such conventional methods have the following problems.

即ち加工食品にたれ液を浸透させる場合濃度の異なるた
れ液中に順次浸漬させて所定濃度のたれ液を含浸させて
いるため、複数の容器を準備しなければならない(第3
図イ〜ホ参照)。
That is, when a processed food is impregnated with a sauce liquid, it is necessary to prepare a plurality of containers because the processed food is sequentially immersed in sauce liquids of different concentrations to impregnate it with a predetermined concentration of the sauce liquid.
(See Figures I to H).

従って、多量のたれ液を必要とする上に広い床面積を確
保する必要がある。
Therefore, in addition to requiring a large amount of dripping liquid, it is also necessary to secure a large floor area.

又各容器内のたれ液に浸漬された食品原料は所定時間浸
漬させた後、順次高濃度の容器へ移し変えられている。
Furthermore, the food ingredients immersed in the dripping liquid in each container are immersed for a predetermined time and then transferred to containers with higher concentrations.

このように食品原料の移し変えに要する設備(例えば第
3図C)及び人手を要すると共に、移し変え時に生ずる
振動等によって食品原料が破損したり、傷がつき商品価
値を喪失する場合があった。
In this way, transferring food ingredients requires equipment (for example, Figure 3 C) and manpower, and the food ingredients may be damaged or scratched due to vibrations generated during transfer, resulting in loss of commercial value. .

さらに各容器内のたれ液は上方が高く下方が低いので加
工食品に与える風味等に差異が生じゃすく又、たれ液濃
度は糖液等の成分が沈澱することによって上方が薄く下
方では濃くなってしまうことにより、加工食品に均一な
味付けが行なえず上下間に品質上の差が生じていた。
Furthermore, since the sauce in each container is higher at the top and lower at the bottom, there is a difference in the flavor imparted to processed foods.In addition, the concentration of the sauce is thinner at the top and thicker at the bottom due to the precipitation of components such as sugar solution. As a result, processed foods cannot be seasoned uniformly, resulting in quality differences between the top and bottom.

その対策として従来は、たれ液中に浸漬した食品原料を
数時間ごとに数回の出し入れを行なって浸漬する食品の
上下を変えたりして、味付けの均−化を図らねばならな
かった。
Conventionally, as a countermeasure to this problem, it was necessary to take the food material immersed in the sauce in and out several times every few hours, changing the top and bottom of the food to be immersed, in order to even out the seasoning.

食品原料から出て来た水分によって薄められたたれ液は
、大気圧下で煮沸して濃縮するため糖液等のたれ液が褐
変し、加工食品を変色させ、又苦味を生じさせるなどの
著しい品質低下を招く等の欠点があり、そのため1度又
は数回使用すると、そのたれ液を廃棄しているのが実情
であった。
The sauce diluted by the water released from the food ingredients is boiled under atmospheric pressure and concentrated, resulting in browning of the sauce such as sugar solution, discoloration of processed foods, and the production of bitter taste. There are drawbacks such as deterioration of quality, and for this reason, the actual situation is that the dripping liquid is discarded after being used once or several times.

又大気圧下で開放して処理をする装置では、この装置を
設置した室内に蒸発蒸気が充満し、温度及び湿度共に上
昇し、作業者の健康上、又は安全性の面からも極めて悪
条件となっていた。
In addition, with equipment that processes in an open environment under atmospheric pressure, the room in which the equipment is installed will be filled with evaporated steam, increasing both temperature and humidity, creating extremely adverse conditions from the health and safety standpoint of workers. It became.

本発明は、上記のような欠点や問題点を解消するため鋭
意研究されたもので、密閉型のたれ液容器を濃縮装置に
組込むことにより極めて合理的且つ、高性能の浸漬装置
を提供したものである。
The present invention has been intensively researched to solve the above-mentioned drawbacks and problems, and provides an extremely rational and high-performance dipping device by incorporating a closed drip container into a concentrating device. It is.

以下、図面に従ってその構成を説明する。The configuration will be explained below according to the drawings.

1は密閉型のたれ液容器で、蓋2を開閉することによっ
て、食品原料3を多数載置した複数のトレイ4を積層し
てなる内槽5を出し入れできるようにしている。
Reference numeral 1 denotes a closed type sauce container, and by opening and closing a lid 2, an inner tank 5 formed by stacking a plurality of trays 4 on which a large number of food ingredients 3 are placed can be taken in and out.

6は前記たれ液容器1内下方に設けられた間接型熱交換
器で、たれ液の昇温、冷却を行なっている。
Reference numeral 6 denotes an indirect heat exchanger provided below the inside of the dripping liquid container 1, which heats and cools the dripping liquid.

7は温水入口弁、8は温水出口弁、9は冷却水入口弁、
10は冷却水出口弁を示す。
7 is a hot water inlet valve, 8 is a hot water outlet valve, 9 is a cooling water inlet valve,
10 indicates a cooling water outlet valve.

11は循環ポンプで、このポンプ11から吐出されたた
れ液は、吐出側配管12から前記たれ液容器1内に装填
された内槽5へ供給される。
11 is a circulation pump, and the dripping liquid discharged from this pump 11 is supplied from a discharge side piping 12 to the inner tank 5 loaded in the dripping liquid container 1.

前記内槽5内に積層されたトレイ4に載置された食品原
料3の間隙を通ったたれ液は、上方から水分を蒸発しな
がら前記たれ液容器1内壁と前記内槽5の外壁との間隙
に流下し、吸込側配管13を通つて、循環ポンプ11へ
還流される。
The dripping liquid that has passed through the gap between the food ingredients 3 placed on the stacked trays 4 in the inner tank 5 evaporates water from above, while the dripping liquid flows between the inner wall of the dripping liquid container 1 and the outer wall of the inner tank 5. It flows down into the gap, passes through the suction side piping 13, and is returned to the circulation pump 11.

14は流量調整弁、15は流量計で、循環たれ液流量を
制御している。
Reference numeral 14 is a flow rate regulating valve, and 15 is a flow meter, which controls the flow rate of the circulating dripping liquid.

16は給液弁、17は排液弁、18はストレーナ、19
は温度感知部を示す。
16 is a liquid supply valve, 17 is a drain valve, 18 is a strainer, 19
indicates the temperature sensing part.

20はコンデンサで、配管21を介して前記たれ液容器
1と連通されている。
20 is a condenser, which is communicated with the dripping liquid container 1 via a pipe 21.

22は間接冷却器で、23は冷却水入口弁、24は冷却
水出口弁を示す。
22 is an indirect cooler, 23 is a cooling water inlet valve, and 24 is a cooling water outlet valve.

25は真空計、26はストップ弁で、前記配管21に付
設されている。
25 is a vacuum gauge, and 26 is a stop valve, which are attached to the piping 21.

従って、前記たれ液容器1内で蒸発した蒸気は、前記コ
ンデンサ20へ送られ、前記間接冷却器22によって凝
縮される。
Therefore, the vapor evaporated in the dripping liquid container 1 is sent to the condenser 20 and condensed by the indirect cooler 22.

27は濃度コントローラで、前記コンデンサ20で凝縮
された凝縮水を配管28を介して貯溜するようになって
いる。
27 is a concentration controller which stores the condensed water condensed in the condenser 20 via a pipe 28.

29は凝縮水の貯溜量を感知するための液位感知部で、
複数の電極棒又はフロート式、その他によって構成され
ている。
29 is a liquid level sensing part for sensing the amount of condensed water stored;
It is composed of multiple electrode rods, float type, etc.

従って、あらかじめ設定された位置で凝縮水の液位が感
知され、前記たれ液容器1内のたれ液濃度がわかるよう
になっている。
Therefore, the liquid level of the condensed water is sensed at a preset position, and the concentration of the dripping liquid in the dripping liquid container 1 can be determined.

30は排液弁を示す。31は循環ポンプ、32はエゼク
タ一部、33は水タンクで、これらを配管34によって
循環路に形成し真空発生装置としている。
30 indicates a drain valve. 31 is a circulation pump, 32 is a part of an ejector, and 33 is a water tank, and these are formed into a circulation path by piping 34 to form a vacuum generating device.

前記コンデンサ20と前記エゼクタ一部32との間は、
配管35によって連通され、前記エゼクタ一部32に生
じた負圧によって前記たれ液容器1内の空気を吸引して
減圧したれ液の蒸発を促進している。
Between the capacitor 20 and the ejector part 32,
They are communicated by a pipe 35, and the negative pressure generated in the ejector part 32 sucks the air inside the dripping liquid container 1 to reduce the pressure and promote evaporation of the dripping liquid.

36は給水弁、37は排液弁である。36 is a water supply valve, and 37 is a drain valve.

濃度コントローラ27の液位感知部29で凝縮水の貯蔵
量が感知されると、手動又は自動によりストップ弁26
を閉止するとたれ液容器1内のたれ液は一定の濃度が保
持される。
When the liquid level sensor 29 of the concentration controller 27 detects the amount of condensed water stored, the stop valve 26 is activated manually or automatically.
When the dripping liquid container 1 is closed, the dripping liquid in the dripping liquid container 1 is maintained at a constant concentration.

又ストップ弁26を開放した時にはコンデンサ20を介
して連通している真空発生装置のエゼクタ一部32によ
り空気が吸入され、たれ液容器1内の蒸発を促がすよう
構成されている。
Furthermore, when the stop valve 26 is opened, air is sucked in by the ejector part 32 of the vacuum generator, which is communicated through the condenser 20, to promote evaporation in the dripping liquid container 1.

尚蒸発の程度は真空発生装置の循環ポンプ31の駆動又
は停止によるか、ストップ弁26の調節によっても行な
うことができる。
The degree of evaporation can be controlled by driving or stopping the circulation pump 31 of the vacuum generator or by adjusting the stop valve 26.

本発明は上記のような構成をとったもので、糖液等のた
れ液容器が1つあれば浸漬処理が十分性なうことができ
、この1つの容器により濃度調整が可能なため準備する
たれ液量が従来法に比べて大巾に(約5分の1)削減す
ることができるようになった。
The present invention has the above-mentioned configuration, and the immersion process can be carried out sufficiently if there is one container for sauce such as sugar solution, and the concentration can be adjusted with this one container. The amount of dripping liquid can now be reduced by a large amount (approximately one-fifth) compared to the conventional method.

又たれ液の昇温、冷却等に要する熱エネルギー及び冷却
水量も少なくてすみ、装置設置面積も極めて狭い所でも
十分可能となった。
Also, the thermal energy and amount of cooling water required for heating and cooling the dripping liquid are small, and the installation area of the device can be sufficiently reduced even in an extremely small place.

又、濃度調整が可能なため食品原料が収納された内槽を
濃度が変化するたびに、出し入れする必要が全くなく従
来法のように出し入れに要する手間が省けるとともに、
出し入れに伴なう振動等によって食品原料が破損したり
、傷つき、商品価値を喪失するという恐れが解消された
In addition, since the concentration can be adjusted, there is no need to take the inner tank containing the food ingredients in and out every time the concentration changes, which saves the time and effort required to put in and take out the food raw materials as in conventional methods.
This eliminates the fear that food ingredients will be damaged or damaged and lose their commercial value due to vibrations caused by loading and unloading.

そして、濃度調整のためには濃度コントロール、ストッ
プ弁、真空発生装置を利用して、容易に且つ正確に制御
できるようになった。
In order to adjust the concentration, it has become possible to easily and accurately control the concentration by using a concentration control, a stop valve, and a vacuum generator.

さらに容器内のたれ液が、たえず循環ポンプによって循
環、攪拌されているので容器内上下間の温度差、濃度差
が解消され、均一な品質の加工食品が得られる。
Furthermore, since the dripping liquid inside the container is constantly circulated and stirred by the circulation pump, differences in temperature and concentration between the upper and lower parts of the container are eliminated, and processed foods of uniform quality can be obtained.

そして、糖液等のたれ液の濃縮は真空低温下で行なわれ
るので、たれ液の褐変現象が皆無となりたれ液の再利用
が可能であると共に、加工食品を変色させず安定した品
質を維持できる等の効果がある。
In addition, since the concentration of sauces such as sugar solutions is carried out under vacuum and low temperature, there is no browning of the sauce, making it possible to reuse the sauce and maintaining stable quality without discoloring processed foods. There are other effects.

さらに密閉型の容器を利用しているため、蒸発蒸気が室
内へ噴出することがなく、作業環境において、従来の大
気開放型と比べて極めて良好となった。
Furthermore, since a closed container is used, evaporated steam does not escape into the room, resulting in a much better working environment compared to conventional open-air containers.

第2図に示したのは、他実施例であり、循環ポンプ11
の吐出側配管12に分岐管38を設け、殺菌器39に連
通させ、液温調節器40を経て、たれ液容器1へたれ液
の一部を供給するようにしたものである。
What is shown in FIG. 2 is another embodiment, in which the circulation pump 11
A branch pipe 38 is provided in the discharge side piping 12 of the drain pipe 12 to communicate with a sterilizer 39, and a part of the dripping liquid is supplied to the dripping liquid container 1 through a liquid temperature regulator 40.

前記殺菌器39は間接熱交換器がらなり約120℃の蒸
気によってたれ液中に存在する菌を殺菌している。
The sterilizer 39 consists of an indirect heat exchanger and uses steam at about 120° C. to sterilize bacteria present in the dripping liquid.

41は仕切弁、42は蒸気入口弁、44はスチームトラ
ップを示す。
41 is a gate valve, 42 is a steam inlet valve, and 44 is a steam trap.

液温調節器40も間接熱交換器からなり冷却水との間接
熱交換によりたれ液を冷却し、たれ液容器1へ還元させ
ている。
The liquid temperature regulator 40 also includes an indirect heat exchanger, and cools the dripping liquid by indirect heat exchange with cooling water, and returns the dripping liquid to the dripping liquid container 1.

44は冷却水入口弁、45は冷却水出口配管、46は仕
切弁を示す。
44 is a cooling water inlet valve, 45 is a cooling water outlet pipe, and 46 is a gate valve.

このように分岐管を設けて、一部たれ液を殺菌すること
により循環たれ液中の菌の増殖を防止し良品質の加工食
品を得る効果がある。
Providing a branch pipe in this manner and partially sterilizing the dripping liquid has the effect of preventing the growth of bacteria in the circulating dripping liquid and obtaining a high-quality processed food.

従って従来法のように、たれ液温度が50〜60℃で処
理され、長時間運転中に菌が増殖し加工後の保存期間が
短かく、且つ品質劣化が生じるような難点は皆無となっ
たみ
Therefore, unlike the conventional method, the temperature of the dripping liquid is 50 to 60℃, and there are no problems such as bacterial growth during long-term operation, short storage period after processing, and quality deterioration. fruit

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

第1図は本発明装置の全体経路を示す要部断面図、第2
図は他実施例を示す要部断面図、第3図は従来例を示す
断面図。 1……密閉型たれ液容器、3……食品原料、4……トレ
イ、5……内槽、6……間接型熱交換器、11……循環
ポンプ、12,13……配管、20……コンデンサ、2
1……配管、26……ストツプ弁、27……濃度コント
ローラ、31……ポンプ、32……エゼクタ一部、33
……水タンク。
Fig. 1 is a cross-sectional view of the main parts showing the entire path of the device of the present invention;
The figure is a sectional view of a main part showing another embodiment, and FIG. 3 is a sectional view showing a conventional example. DESCRIPTION OF SYMBOLS 1... Sealed dripping liquid container, 3... Food raw material, 4... Tray, 5... Inner tank, 6... Indirect heat exchanger, 11... Circulation pump, 12, 13... Piping, 20... ...Capacitor, 2
1... Piping, 26... Stop valve, 27... Concentration controller, 31... Pump, 32... Part of ejector, 33
……water tank.

Claims (1)

【特許請求の範囲】[Claims] 1 食品原料を載置したトレイの複数個を積層した内槽
を取出自在に装填した密閉型たれ液容器と、この容器内
の下方部に設けた間接型熱交換器と、前記容器内のたれ
液を循環させるよう配管を介して設けた循環ポンプと、
前記容器内で発生する蒸発蒸気を凝縮するためストップ
弁と配管を介して設けたコンデンサと、このコンデンサ
で生じた凝縮液を貯溜し、液位感知部と連動してたれ液
の濃度を調整するために設けた濃度コントローラと、前
記コンデンサ上端と連通ずるエゼクタ一部、水タンク、
ポンプ等を配管で連結した液循環路を有する真空発生装
置とから成り、濃度コントローラと真空発生装置とによ
り調整されたたれ液濃度を保持しつつ循環ポンプにより
容器中のたれ液を循環させるようにしたことを特徴とす
る糖液等のたれ液循環濃度浸漬装置。
1. A sealed dripping liquid container removably loaded with an inner tank in which a plurality of stacked trays carrying food ingredients are loaded, an indirect heat exchanger installed in the lower part of this container, and a dripping liquid container in the container. A circulation pump installed via piping to circulate the liquid,
A condenser is provided via a stop valve and piping to condense the evaporated steam generated in the container, and the condensate generated in this condenser is stored, and the concentration of the dripping liquid is adjusted in conjunction with the liquid level sensing part. a concentration controller provided for the purpose, a part of the ejector communicating with the upper end of the capacitor, a water tank,
It consists of a vacuum generator having a liquid circulation path connected to a pump etc. by piping, and the circulation pump circulates the dripping liquid in the container while maintaining the dripping liquid concentration adjusted by the concentration controller and the vacuum generator. A dipping device for circulating and concentrating a dripping liquid such as a sugar solution.
JP54117019A 1979-09-11 1979-09-11 Sauce circulation concentration dipping equipment for sugar solutions, etc. Expired JPS5811984B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP54117019A JPS5811984B2 (en) 1979-09-11 1979-09-11 Sauce circulation concentration dipping equipment for sugar solutions, etc.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP54117019A JPS5811984B2 (en) 1979-09-11 1979-09-11 Sauce circulation concentration dipping equipment for sugar solutions, etc.

Publications (2)

Publication Number Publication Date
JPS5642551A JPS5642551A (en) 1981-04-20
JPS5811984B2 true JPS5811984B2 (en) 1983-03-05

Family

ID=14701425

Family Applications (1)

Application Number Title Priority Date Filing Date
JP54117019A Expired JPS5811984B2 (en) 1979-09-11 1979-09-11 Sauce circulation concentration dipping equipment for sugar solutions, etc.

Country Status (1)

Country Link
JP (1) JPS5811984B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2665825B2 (en) * 1990-11-27 1997-10-22 東邦シートフレーム株式会社 Cooking food production equipment
JPH0771449B2 (en) * 1991-12-20 1995-08-02 株式会社小倉屋柳本 Tsukudani manufacturing method
JPH0646748A (en) * 1992-07-27 1994-02-22 M Y Eng:Kk Vacuum cooking device
US6742618B2 (en) 2000-03-07 2004-06-01 Arctic Cat, Inc. Snowmobile planetary drive system
US6907951B2 (en) 2000-03-07 2005-06-21 Arctic Cat, Inc. Snowmobile planetary drive system
JP2008193915A (en) * 2007-02-09 2008-08-28 Musashino Corp Seasoning liquid feeder
JP5579788B2 (en) * 2012-06-22 2014-08-27 株式会社日阪製作所 Seasoning method of food

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