JPS5912724A - Recirculation type purification of oil of fryer - Google Patents

Recirculation type purification of oil of fryer

Info

Publication number
JPS5912724A
JPS5912724A JP12126682A JP12126682A JPS5912724A JP S5912724 A JPS5912724 A JP S5912724A JP 12126682 A JP12126682 A JP 12126682A JP 12126682 A JP12126682 A JP 12126682A JP S5912724 A JPS5912724 A JP S5912724A
Authority
JP
Japan
Prior art keywords
oil
fryer
fine particles
circulating oil
recirculated
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.)
Pending
Application number
JP12126682A
Other languages
Japanese (ja)
Inventor
Shuji Miyabayashi
宮林 修二
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 Kakoki Kaisha Ltd
Original Assignee
Mitsubishi Kakoki Kaisha 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 Kakoki Kaisha Ltd filed Critical Mitsubishi Kakoki Kaisha Ltd
Priority to JP12126682A priority Critical patent/JPS5912724A/en
Publication of JPS5912724A publication Critical patent/JPS5912724A/en
Pending legal-status Critical Current

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

PURPOSE:To suppress the oxidation of oil, by separating and removing fine particles in recirculated oil by electrostatic filtration to remove extemely fine particles. CONSTITUTION:The oil 2 in a fryer 1 heated by a burner 3 is taken out by opening the valve 5 of the arranged pipe 4 provided to the bottom part of the fryer 1 and the taken out recirculated oil is passed through a strainer 6 to remove coarse particles therein. The coarse particle removed oil is sent to a thin film evaporator 9 through an arranged pipe 8 by a pump 7 to remove moisture in the recirculated oil. The removed moisture is sent to a condenser 14 from an arranged pipe 13 and discharged to a discharge pipe 16 as condensed water. The dehydrated recirculated oil is introduced into an electrostatic filter 11 by an arranged pipe 10 and carbonized fine particles in the oil are attracted to and collected by the anode in the electrostatic filter 11. Purified recirculated oil is returned to the fryer 1 from an arranged pipe 12.

Description

【発明の詳細な説明】 本発明は油で揚げた食品を商業的に製造するフライヤに
関し、特にフライヤの使用中に油中に生成する揚滓や炭
化物を連続的に除去する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a fryer for commercially producing fried foods, and more particularly to a method for continuously removing fried scum and chars generated in oil during use of the fryer. .

フライヤによって食品を揚げている際に発生する・揚滓
および炭化物は、揚製品に付着してその品質を劣化し、
商品価値を低下せしめるのみでなく、油の酸化を早めて
油の性質を悪化せしめ、また油の酸化分解によるアクロ
レイン等の揮発性化合物が作業現場の環境を悪化せしめ
る。従って、フライヤではその使用中に油の一部を常時
抜出して、その油中に含まれている揚滓や炭化物を分離
してから再びフライヤ中に戻すという方法で、油の浄化
が行われているが、現在市販されているフライヤは、発
生する揚滓や炭化物を簡単なフィルタで漣過しているだ
けで、揚製品の品質や油の酸化に影響を与える粒径が2
〜10μの微粒子を除去することは困難である。フィル
タとして焼結金属等の目の細かいものを使用して濾過を
行う場合は、度が大である。
The slag and charred substances generated when frying foods in a fryer adhere to fried products and deteriorate their quality.
Not only does this reduce the product value, but it also accelerates the oxidation of the oil and deteriorates its properties, and the volatile compounds such as acrolein produced by the oxidative decomposition of the oil deteriorate the environment at work sites. Therefore, during use of a fryer, oil is purified by constantly drawing out a portion of the oil, separating the slag and charred substances contained in the oil, and then returning it to the fryer. However, currently commercially available fryers simply filter the fried slag and charred matter through a simple filter, but the particle size is 2.
It is difficult to remove particles of ~10μ. When filtration is performed using a fine mesh material such as sintered metal as a filter, the degree of filtering is large.

本発明はフライヤにおける油の揚滓および炭化物を、少
ない圧力損失で、極めて微粒子の炭化物まで除去するこ
とができ、油の酸化を防いで油の寿命を延ばすと共に、
炭化微粒子の除去による揚製品の品質を向」二せしめる
、フライヤの循環式浄油力法を提[共するものである1
、 即ち本発明は、加熱された7ライヤ中の油の一部を俵出
し、油中の粒子を除去した後フライヤ中に再循環せしめ
る、循環式浄油方法において、循環油中の判1粒子を除
去した後、薄膜式蒸発によって循環油中の水分を除去し
、次いて循環油に静電圧を印加し、循環油中の微粒子を
静電捕集し、浄化された循環油をフライヤ中に戻すこと
を特徴とする、フライヤの循環式浄油方法である。
The present invention can remove oil slag and carbide in a fryer with little pressure loss, down to extremely fine particles of carbide, prevent oil oxidation, extend the life of the oil,
We propose a circulating oil purification method for fryers that improves the quality of fried products by removing carbonized particles.
That is, the present invention provides a circulating oil purification method in which a portion of the oil in a heated 7-ryer is drained into bales, particles in the oil are removed, and then recirculated into a fryer. After removing the water, water in the circulating oil is removed by thin film evaporation, and then an electrostatic voltage is applied to the circulating oil to electrostatically collect fine particles in the circulating oil, and the purified circulating oil is placed in a fryer. This is a circulation-type oil purification method for fryers, which is characterized by returning the oil.

以下、本発明の方法をその一実施例を示す図面に基づい
て詳細に説明する。
Hereinafter, the method of the present invention will be explained in detail based on the drawings showing one embodiment thereof.

第1図は本発明のフライヤ浄油方法を具体的に実施する
場合の一例を示すフライヤ循環浄油装置のフローシート
である。
FIG. 1 is a flow sheet of a fryer circulation oil purification apparatus showing an example of a concrete implementation of the fryer oil purification method of the present invention.

リンダバーナ6て加熱されたフライヤ1中の油2は、フ
ライヤ1の底部の配管4のバルブ5を開けることによっ
て取出され、取出された循環油はストレーナ乙によって
粗粒子が除去される。ストレーナ6中に設けられた網は
メツシュが40〜80程度で、これは次のポンプ7の目
詰り防止と後段における微粒子除去の際の負荷を軽くし
、かつ、除去効果をあげるためのものである。粗粒子の
除去された循環油は、ポンプ7により配管8を経て薄膜
蒸発器9に送られる。薄膜蒸発器は任意の形式が採用し
得るが、本発明において用いられる薄膜蒸発器は循環油
中に分散している水分を除去することを目的とし、導入
される循環油は既に水の沸点以」二の高温に加熱されて
いるので、薄膜蒸発に際して特に加熱する必要がなく、
ポ°ンプアップされた循環油が分離板に衝突し、薄膜状
で流下する形式かとられる。第2図はそのような薄膜式
蒸発器の一例を示し、円錐状の分離板21および22を
順次流下する形式のものである。循環油中の水分は、循
環前が薄膜化されることにより、高温の油のためにカス
化され、数段の分離板を流下することでほぼ完全に水分
は循環油から分離される。
The oil 2 in the fryer 1 heated by the cylinder burner 6 is taken out by opening the valve 5 of the pipe 4 at the bottom of the fryer 1, and the coarse particles of the taken out circulating oil are removed by the strainer B. The mesh installed in the strainer 6 has a mesh size of about 40 to 80, and this is to prevent clogging of the next pump 7, to lighten the load when removing particulates in the subsequent stage, and to increase the removal effect. be. The circulating oil from which coarse particles have been removed is sent to a thin film evaporator 9 via a pipe 8 by a pump 7. Although any type of thin film evaporator can be adopted, the purpose of the thin film evaporator used in the present invention is to remove water dispersed in circulating oil, and the circulating oil introduced has already reached a temperature higher than the boiling point of water. Because it is heated to a high temperature, there is no need for special heating during thin film evaporation.
The pumped-up circulating oil collides with the separation plate and flows down in a thin film. FIG. 2 shows an example of such a thin film evaporator, in which water flows successively through conical separation plates 21 and 22. Moisture in the circulating oil is formed into a thin film before circulation, which turns it into scum due to the high temperature of the oil, and water is almost completely separated from the circulating oil by flowing down several stages of separation plates.

薄膜式蒸発器としては、第2図に示した形式の他、通常
用いられる円筒の内面または外面を薄膜状で流下する形
式のものも採用し得る。
In addition to the type shown in FIG. 2, the thin film type evaporator may also be of a type in which a thin film flows down the inner or outer surface of a commonly used cylinder.

放出された水蒸気は、薄膜式蒸発器9の上部から配管1
3を経て凝縮器14で凝縮され、凝縮水はバルブ15を
経て排水管16へ排出される。
The released water vapor flows from the top of the thin film evaporator 9 to the pipe 1.
3, the condensed water is condensed in a condenser 14, and the condensed water is discharged to a drain pipe 16 via a valve 15.

薄膜蒸発器9て脱水された循環油は、配管10により静
電濾過器11へ導入される。静電濾過器11は循環油の
収容された容器中に電極を備え、陽極とし、容器を陰極
として設置する。両極間に5〜50kVの直流電圧が印
加されている。この印加電圧による電界により、循環油
中の荷電された微細粒子は、その有する静電気の種類に
応して、その対極へ吸引される。一般に油中に分散する
微粒子は負に荷電されているので、循環油中の炭化微粒
子は静電濾過器中の1湯極に吸引されて捕集される。
The circulating oil dehydrated in the thin film evaporator 9 is introduced into an electrostatic filter 11 through a pipe 10. The electrostatic filter 11 is provided with an electrode in a container containing circulating oil, which serves as an anode, and the container is installed as a cathode. A DC voltage of 5 to 50 kV is applied between both poles. Due to the electric field caused by this applied voltage, the charged fine particles in the circulating oil are attracted to the opposite electrode depending on the type of static electricity they have. Since the fine particles dispersed in oil are generally negatively charged, the carbonized fine particles in the circulating oil are attracted to and collected by the hot water electrode in the electrostatic filter.

第3図はそのような静電濾過器の1例の横断面図を示し
、円筒容器31それ自体を陰極とし、中心に陽極32を
設けたもので、陽極の周囲をひだをつけたp紙36で囲
んでいる。容器中に導入された循環油中の微粒子は、両
極に印加された高電圧により陽極へと泳動し、p紙36
上に捕集されるので、捕集された微粒子は、必要に応じ
てp紙33を交換することによって容易に処分すること
ができる。
FIG. 3 shows a cross-sectional view of an example of such an electrostatic filter, in which a cylindrical container 31 itself is used as a cathode, an anode 32 is provided in the center, and the anode is surrounded by pleated P paper. It is surrounded by 36. Fine particles in the circulating oil introduced into the container migrate to the anode due to the high voltage applied to both poles, and
Since the fine particles are collected on the top, the collected fine particles can be easily disposed of by replacing the p paper 33 as necessary.

静電濾過においては、油中に水分の含有が多いと、両極
に印加された静電圧の短絡を生し易く、分散微粒子の捕
集効率が低下するので、静電濾過の前に薄膜蒸発器9に
よる水分除去を充分に行うことが必要である。
In electrostatic filtration, if oil contains a large amount of water, the electrostatic voltage applied to both poles is likely to short-circuit, reducing the collection efficiency of dispersed particles. Therefore, a thin film evaporator is used before electrostatic filtration. It is necessary to sufficiently remove water by step 9.

水分除去された循環油は、静電濾過器11に好ましくは
下部から導入され、静電濾過されて清浄となった循環油
は静電汗過器11の−1一部より取出し、配管11によ
ってフライヤ1中に戻される。
The circulating oil from which water has been removed is preferably introduced into the electrostatic filter 11 from the lower part, and the circulating oil that has been electrostatically filtered and becomes clean is taken out from the -1 part of the electrostatic sweat filter 11 and passed through the pipe 11. Returned to Flyer 1.

薄膜蒸発器9から静電濾過器11への循環油の移動およ
び静電濾過器11からフライヤへの戻しは、いずれも重
力による自然流下によって行うことができ、その場合は
、それぞれ必要な落差を設ける必要がある。この移動は
勿論ポンプ等によることもできる。
The movement of the circulating oil from the thin film evaporator 9 to the electrostatic filter 11 and the return from the electrostatic filter 11 to the fryer can both be performed by gravity flow, and in that case, the necessary head for each can be achieved. It is necessary to provide Of course, this movement can also be done using a pump or the like.

本発明の浄化方法は、微粒子の除去を静電濾過によって
行うため、微粒子の目詰りによる圧力損失がなく、従っ
て長時間の連続運転が可能である。
In the purification method of the present invention, since particulates are removed by electrostatic filtration, there is no pressure loss due to clogging of particulates, and therefore continuous operation for a long time is possible.

また、循環油中の微粒子の除去が静電方式であるため、
極めて微細な粒子まで除去されるので、油の酸化か少な
く、揚411のか命か延びると共に、酸fヒに汁なうア
クロレイン等の刺戟性揮発物の発生が少なく、作業環境
か改善される。また、揚製品の品質を低下させる炭化微
粒子が除去されるので、一定の品質の揚製品を作ること
かできる。
In addition, since particulates in the circulating oil are removed using an electrostatic method,
Since even extremely fine particles are removed, there is less oxidation of the oil, extending the life of the fryer, and there is less generation of irritating volatile substances such as acrolein, which are absorbed by acids, improving the working environment. Furthermore, since carbonized fine particles that degrade the quality of fried products are removed, fried products of constant quality can be produced.

本発明の方法は、揚油中に生ずるWl、細な炭化粒子を
効果的に除去することができるあて、微粒子の揚滓の発
生する揚製品、例えばカリン糖、米菓、揚パン、ドーナ
ツ、その他スナック菓子の製造に際して特に有効である
The method of the present invention can effectively remove Wl and fine carbonized particles generated during frying, and can be applied to fried products that generate fine particles such as quince sugar, rice crackers, fried bread, donuts, etc. It is particularly effective in the production of snack foods.

実施例1 第1図に示す装置を用い、油として大豆白絞油を1so
°cに加熱した。パン粉と小麦粉を重量比で6°4て混
合したものを、油に対して0.35重量%をフライヤ中
に投入し、循環浄油を行った。
Example 1 Using the apparatus shown in Figure 1, 1 soybean white squeezed oil was used as oil.
heated to °C. A mixture of bread crumbs and wheat flour at a weight ratio of 6°4 was put into a fryer in an amount of 0.35% by weight based on oil, and circulating oil purification was performed.

静電濾過器より7ライヤへ戻される油を検査したところ
、油中には微粒子の存在は殆んど詔められなかった。一
方、浄油前の同じ油をp紙で沖過したところ、7〜8μ
の粒子が残存していることか認められた。
When the oil returned to the 7-Lier from the electrostatic filter was inspected, it was found that there were almost no particulates in the oil. On the other hand, when the same oil before oil purification was passed through P paper, the result was 7 to 8 μm.
It was observed that some particles remained.

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

第1図は本発明の浄油方法の実施例を示すフローシート
である。第2図は薄膜蒸発器の1例の断面図、第3図は
静電濾過器の1例の横断面図である0 図示された要部と符号との対応は次のとおりである。 1 フライヤ、  2・揚油、  ろ リングバーナ、
 6 ストレーナ、  7・ポンプ、 9・・薄膜蒸発
器、  11 静電濾過器、 14・・凝縮器、21.
22 分離板、 31・円筒容器(陰極)、ろ2・陽極
、 36 P紙。 代理人 弁理士厚田桂一部
FIG. 1 is a flow sheet showing an embodiment of the oil purification method of the present invention. FIG. 2 is a cross-sectional view of an example of a thin film evaporator, and FIG. 3 is a cross-sectional view of an example of an electrostatic filter. 1 fryer, 2 frying oil, filter ring burner,
6 Strainer, 7. Pump, 9. Thin film evaporator, 11 Electrostatic filter, 14. Condenser, 21.
22 Separation plate, 31 Cylindrical container (cathode), Filter 2 Anode, 36 P paper. Agent: Patent Attorney Katsura Atsuta

Claims (1)

【特許請求の範囲】[Claims] (1)加熱されたフライヤ中の油の一部を抜出し、油中
の粒子を除去した後フライヤ中に再循環せしめる、循環
式浄油方法において、循環油中の粗粒子を除去した後、
薄膜式蒸発によって循環油中の水分を除去し、次いで循
環油に静電圧を印加し、循環油中の微粒子を静電捕集し
、浄化された循環油をフライヤ中に戻すことを特徴とす
る、フライヤの循環式浄油方法。
(1) In a circulating oil purification method in which a portion of the oil in the heated fryer is extracted, particles in the oil are removed, and then recirculated into the fryer, after coarse particles in the circulating oil are removed,
It is characterized by removing water in the circulating oil by thin film evaporation, then applying an electrostatic voltage to the circulating oil to electrostatically collect fine particles in the circulating oil, and returning the purified circulating oil to the fryer. , Circulating oil purification method for fryers.
JP12126682A 1982-07-14 1982-07-14 Recirculation type purification of oil of fryer Pending JPS5912724A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12126682A JPS5912724A (en) 1982-07-14 1982-07-14 Recirculation type purification of oil of fryer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12126682A JPS5912724A (en) 1982-07-14 1982-07-14 Recirculation type purification of oil of fryer

Publications (1)

Publication Number Publication Date
JPS5912724A true JPS5912724A (en) 1984-01-23

Family

ID=14806992

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12126682A Pending JPS5912724A (en) 1982-07-14 1982-07-14 Recirculation type purification of oil of fryer

Country Status (1)

Country Link
JP (1) JPS5912724A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009273897A (en) * 2004-10-06 2009-11-26 Rie Usui Fryer

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009273897A (en) * 2004-10-06 2009-11-26 Rie Usui Fryer

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