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JP2003284506A - Method for drying food dregs - Google Patents

Method for drying food dregs

Info

Publication number
JP2003284506A
JP2003284506A JP2002089725A JP2002089725A JP2003284506A JP 2003284506 A JP2003284506 A JP 2003284506A JP 2002089725 A JP2002089725 A JP 2002089725A JP 2002089725 A JP2002089725 A JP 2002089725A JP 2003284506 A JP2003284506 A JP 2003284506A
Authority
JP
Japan
Prior art keywords
drying
heating
food
dried
superheated steam
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.)
Withdrawn
Application number
JP2002089725A
Other languages
Japanese (ja)
Inventor
Hisatoshi Wakabayashi
久幹 若林
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP2002089725A priority Critical patent/JP2003284506A/en
Publication of JP2003284506A publication Critical patent/JP2003284506A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/80Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
    • Y02P60/87Re-use of by-products of food processing for fodder production

Landscapes

  • Drying Of Solid Materials (AREA)
  • Processing Of Solid Wastes (AREA)
  • Fodder In General (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for drying food dregs by which valuable dried resources are obtained in a short time without causing scorches. <P>SOLUTION: The method for drying food dregs comprises repeating dry and moisturization of food dregs through subjecting the dregs to superheated steam heating until the food dregs have a limiting moisture content, and subjecting the dried and moisturized food dregs to high temperature air heating or indirect heating so as to dry them. <P>COPYRIGHT: (C)2004,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、食品滓から有価な
乾燥資源を得るための乾燥処理方法に関する。
TECHNICAL FIELD The present invention relates to a drying treatment method for obtaining valuable drying resources from food dregs.

【0002】[0002]

【従来の技術】おから、ジュース滓、焼酎滓などの食品
滓を乾燥させて家畜の飼料などに有効利用することが知
られている。例えば、特開2000−189132号公
報には、圧搾された食品滓を蒸気または湯で加熱湿潤
後、加熱乾燥することにより、焦げの無い十分かつ均一
に乾燥された乾燥資源が得られることが記載されてい
る。
2. Description of the Related Art It is known that food slag such as okara, juice slag, and shochu slag are dried and effectively used as feed for livestock. For example, JP-A-2000-189132 describes that a dried and sufficiently dried resource without charring can be obtained by heating and squeezing a pressed food slag with steam or hot water, and then heating and drying. Has been done.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、前記公
報記載の処理方法では、食品滓のストレス開放を目的と
して一度蒸気または湯で加熱湿潤させるために、当然食
品滓の含水率が大幅に増加する。したがって、これを乾
燥するためには含水率が増加した分だけ乾燥時間を延ば
さなければならない。また、焦げを発生させないために
加熱温度を高めることができないので、長時間の乾燥処
理が必要となる。
However, according to the treatment method described in the above publication, the moisture content of the food slag is significantly increased because the food slag is heated and moistened once with the purpose of releasing stress from the food slag. Therefore, in order to dry it, it is necessary to extend the drying time by the amount corresponding to the increase in the water content. Moreover, since the heating temperature cannot be raised because charring does not occur, a long drying process is required.

【0004】そこで、本発明は、食品滓を焦がすことな
く短時間の乾燥処理により有価な乾燥資源を得ることが
できる食品滓の乾燥処理方法を提供するものである。
Therefore, the present invention provides a method for drying food slag that can obtain valuable drying resources by a short drying process without burning the food slag.

【0005】[0005]

【課題を解決するための手段】本発明の食品滓乾燥処理
方法は、食品滓を過熱水蒸気加熱により湿潤および乾燥
を行った後、湿潤および乾燥した食品滓を高温空気加熱
または間接加熱により乾燥を行うことを特徴とする。
Means for Solving the Problems The food slag drying treatment method of the present invention is to wet and dry the food slag by superheated steam heating, and then dry the wet and dried food slag by high temperature air heating or indirect heating. It is characterized by performing.

【0006】過熱水蒸気加熱による湿潤および乾燥は、
限界含水率に達するまで行う。なお、過熱水蒸気加熱に
よる湿潤および乾燥、前記高温空気加熱による乾燥に間
接加熱を併用することができる。
Wetting and drying by heating with superheated steam is
Repeat until the critical moisture content is reached. In addition, indirect heating can be used in combination for wetting and drying by heating with superheated steam and drying by heating with high temperature air.

【0007】[0007]

【発明の実施の形態】本発明において使用する過熱水蒸
気は、熱放射性ガスであり、対流および放射伝熱により
食品滓の加熱、乾燥を行う。過熱水蒸気は、凝縮性ガス
であり、乾燥初期に被乾燥物の食品滓表面で一時的に凝
縮が生じ、内部まで急速に加熱、湿潤することができ
る。
BEST MODE FOR CARRYING OUT THE INVENTION The superheated steam used in the present invention is a heat-radiative gas, and heats and dries the food slag by convection and radiative heat transfer. The superheated steam is a condensable gas, and temporarily condenses on the surface of the food slag of the material to be dried at the initial stage of drying, and can rapidly heat and wet the inside.

【0008】また、過熱水蒸気は、気流中に酸素を含ま
ないため、食品滓を酸化せずに乾燥することができると
ともに、過熱水蒸気は殺菌作用があり、乾燥中に食品滓
中の菌を殺菌することができる。
[0008] Further, since superheated steam does not contain oxygen in the air stream, it is possible to dry the food slag without oxidizing it, and the superheated steam has a bactericidal action and sterilizes the bacteria in the food slag during drying. can do.

【0009】図1(a)は含水率と被乾燥物温度の関係
を示すグラフ、(b)は乾燥速度と含水率との関係を示
すグラフである。本発明において、過熱水蒸気加熱によ
る湿潤および乾燥を限界含水率に達するまで行うのは、
図1に示すように、限界含水率に達するまでの定率乾燥
期間においては入熱がすべて乾燥のために消費されるた
め、食品滓の温度は加熱媒体の温度によらず動的平衡温
度(ほぼ加熱媒体の湿球温度)で推移し、その後の減率
乾燥期間においては入熱の一部が食品滓の加熱に使われ
るために温度が上昇するためである。温度が上昇し過ぎ
て焦げが発生すると乾燥資源としての価値が低下する。
FIG. 1A is a graph showing the relationship between the water content and the temperature of the material to be dried, and FIG. 1B is a graph showing the relationship between the drying rate and the water content. In the present invention, wetting and drying by heating with superheated steam until reaching the limit water content is
As shown in Fig. 1, since the heat input is entirely consumed for drying during the constant rate drying period until the critical moisture content is reached, the temperature of the food dregs does not depend on the temperature of the heating medium, and the dynamic equilibrium temperature (approximately It is because the wet-bulb temperature of the heating medium) changes, and during the subsequent rate-decreasing drying, the temperature rises because part of the heat input is used to heat the food slag. If the temperature rises too much and charring occurs, the value as a drying resource decreases.

【0010】図2は、本発明の食品滓乾燥処理方法のシ
ステムを示す図である。図1において、第1の乾燥機1
で食品滓aが過熱水蒸気cにより湿潤,乾燥される。過
熱水蒸気の温度は、高温であるほど効果が大であり、2
00℃〜500℃の範囲で含水量に応じて設定する。第
2の乾燥機2で第1の乾燥機1で乾燥された食品滓aは
高温空気dにより乾燥され乾燥物bとなる。高温空気の
温度は、100℃以下でよい。
FIG. 2 is a diagram showing a system of the method for drying and processing food slag of the present invention. In FIG. 1, the first dryer 1
The food slag a is wetted and dried by the superheated steam c. The higher the temperature of superheated steam, the greater the effect.
It is set in the range of 00 ° C to 500 ° C according to the water content. The food dregs a dried by the first drier 1 in the second drier 2 is dried by the hot air d to become a dried product b. The temperature of the hot air may be 100 ° C or lower.

【0011】なお、乾燥機には、公知の乾燥機が使用で
き、例えば、チューブ内に食品滓を撹拌しながら搬送す
る複数の撹拌羽根を備えたシャフトが配置され、チュー
ブ外側に形成したジャケットおよびシャフト内部に水蒸
気を流して間接加熱する方式の乾燥機を使用することが
できる。間接加熱を併用すれば、乾燥時間がより短縮さ
れる。
A known dryer can be used as the dryer. For example, a shaft provided with a plurality of stirring blades for conveying the food slag while stirring is arranged in the tube, and a jacket formed outside the tube and It is possible to use a dryer in which steam is flowed inside the shaft to indirectly heat the shaft. If the indirect heating is also used, the drying time can be shortened further.

【0012】[0012]

【実施例】図3(a)は時間と含水率の関係を示すグラ
フ、(b)は時間と被乾燥物温度の関係を示すグラフで
ある。
EXAMPLE FIG. 3 (a) is a graph showing the relationship between time and water content, and FIG. 3 (b) is a graph showing the relationship between time and the temperature of the material to be dried.

【0013】本発明の実施例では、第1の乾燥機に含水
率80%のおからを供給し、300℃の過熱水蒸気を吹
き込み、加熱水蒸気および100℃の間接加熱用蒸気で
湿潤,加熱して乾燥し、限界含水率到達以降に第2の乾
燥機で100℃の高温空気および100℃の間接加熱用
蒸気で加熱して乾燥させた。
In the embodiment of the present invention, the first dryer was supplied with soybean curd having a water content of 80%, superheated steam of 300 ° C. was blown into it, and it was wet and heated with heated steam and steam for indirect heating at 100 ° C. After reaching the critical moisture content, it was heated and dried in the second dryer with high temperature air at 100 ° C and steam for indirect heating at 100 ° C.

【0014】比較例として、第1の乾燥機に含水率80
%のおからを供給し、100℃の湿潤用蒸気を吹き付
け、湿潤した後、100℃の高温空気および100℃の
間接加熱用蒸気で加熱して乾燥させた。
As a comparative example, the first dryer has a water content of 80.
% Of okara was supplied, and steam for wetting at 100 ° C. was sprayed to wet, and then heated by hot air at 100 ° C. and steam for indirect heating at 100 ° C. to be dried.

【0015】図3に示すように、本発明では、300℃
の過熱水蒸気により含水率は限界含水率まで短時間で急
激に下がり(図3(a)参照)、乾燥物温度が限界含水
率に達する時間まで急激に上昇し一定温度で推移した
(図3(b)参照)。限界含水率に達した後、高温空気
の乾燥により、最終目標の含水率まで短時間で乾燥する
ことができ、焦げも見られなかった。
In the present invention, as shown in FIG.
The water content of the superheated steam drastically decreased to the critical water content in a short time (see Fig. 3 (a)), and increased rapidly until the temperature of the dried product reached the critical water content and remained constant (Fig. 3 ( See b)). After reaching the critical moisture content, it was possible to dry to the final target moisture content in a short time by drying the hot air, and no charring was observed.

【0016】本発明に対して比較例では、100℃の高
温空気では限界含水率まで含水率の低下が緩やかで(図
3(a)参照)、乾燥物温度が限界含水率に達する時間
まで低い温度で推移した(図3(b)参照)。限界含水
率に達した後、高温空気の乾燥により、最終目標の含水
率まで乾燥するのに長い時間を要した。
In comparison with the present invention, in the comparative example, in the high temperature air of 100 ° C., the decrease of the water content was slow to the limit water content (see FIG. 3 (a)), and it was low until the temperature of the dried product reached the water content limit. The temperature was changed (see FIG. 3 (b)). After reaching the critical moisture content, drying the hot air took a long time to dry to the final target moisture content.

【0017】図3に示すグラフから明らかなとおり、本
発明は、比較例に比べ、短時間で目標含水率まで乾燥さ
せることができた。
As is clear from the graph shown in FIG. 3, the present invention was able to dry to the target water content in a shorter time than the comparative example.

【0018】[0018]

【発明の効果】従来技術の場合、蒸気または湯により食
品滓を湿潤させた後、高温空気及び間接加熱により乾燥
を行うため長時間の乾燥処理が必要となるが、本発明に
よれば、前段に過熱水蒸気加熱を適用することにより、
短時間での乾燥処理が可能となる。 また、焦げ、酸化
及び保有菌のない高品質で有価な乾燥資源が得られる。
さらに、排蒸気の再循環使用が可能であるため省エネル
ギーが可能となる。
In the case of the prior art, after the food slag is moistened with steam or hot water, a long drying process is required to perform drying by high temperature air and indirect heating. By applying superheated steam heating to
A drying process can be performed in a short time. In addition, a high-quality and valuable dry resource free from charring, oxidization, and retained bacteria can be obtained.
Further, since the exhaust steam can be recycled and used, energy can be saved.

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

【図1】(a)は含水率と被乾燥物温度の関係を示すグ
ラフ、(b)は乾燥速度と含水率との関係を示すグラフ
である。
FIG. 1A is a graph showing the relationship between water content and the temperature of a material to be dried, and FIG. 1B is a graph showing the relationship between drying rate and water content.

【図2】本発明の食品滓乾燥処理方法のシステムを示す
図である。
FIG. 2 is a diagram showing a system of a food dregs drying treatment method of the present invention.

【図3】(a)は時間と含水率の関係を示すグラフ、
(b)は時間と被乾燥物温度の関係を示すグラフであ
る。
FIG. 3 (a) is a graph showing the relationship between time and water content,
(B) is a graph which shows the relationship between time and a to-be-dried material temperature.

【符号の説明】[Explanation of symbols]

1:第1の乾燥機 2:第2の乾燥機 a:食品滓 b:乾燥物 c:過熱水蒸気 d:高温空気 1: First dryer 2: Second dryer a: food waste b: dried product c: Superheated steam d: hot air

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】食品滓を過熱水蒸気加熱により湿潤および
乾燥を行った後、湿潤および乾燥した食品滓を高温空気
加熱により乾燥を行うことを特徴とする食品滓乾燥処理
方法。
1. A method of drying food slag, which comprises heating and drying the food slag by heating with superheated steam, and then drying the wet and dried food slag by heating with high temperature air.
【請求項2】食品滓を過熱水蒸気加熱により湿潤および
乾燥を行った後、湿潤および乾燥した食品滓を間接加熱
により乾燥を行うことを特徴とする食品滓乾燥処理方
法。
2. A food slag drying treatment method, which comprises moistening and drying a food slag by heating with superheated steam, and then drying the wet and dried food slag by indirect heating.
【請求項3】過熱水蒸気加熱による湿潤および乾燥を限
界含水率に達するまで行うことを特徴とする請求項1ま
たは2記載の食品滓乾燥処理方法。
3. The food waste drying method according to claim 1 or 2, wherein the wetting and drying by heating with superheated steam is performed until the moisture content reaches a limit.
【請求項4】前記過熱水蒸気加熱による湿潤および乾燥
に間接加熱を併用することを特徴とする請求項1,2ま
たは3記載の食品滓乾燥処理方法。
4. The method for drying food slag according to claim 1, wherein indirect heating is used in combination with said wetting and drying by heating with superheated steam.
【請求項5】前記高温空気加熱による乾燥に間接加熱を
併用することを特徴とする請求項1、3または4記載の
食品滓乾燥処理方法。
5. The food waste drying method according to claim 1, 3 or 4, wherein indirect heating is used together with the drying by the high temperature air heating.
JP2002089725A 2002-03-27 2002-03-27 Method for drying food dregs Withdrawn JP2003284506A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002089725A JP2003284506A (en) 2002-03-27 2002-03-27 Method for drying food dregs

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002089725A JP2003284506A (en) 2002-03-27 2002-03-27 Method for drying food dregs

Publications (1)

Publication Number Publication Date
JP2003284506A true JP2003284506A (en) 2003-10-07

Family

ID=29235234

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002089725A Withdrawn JP2003284506A (en) 2002-03-27 2002-03-27 Method for drying food dregs

Country Status (1)

Country Link
JP (1) JP2003284506A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008136448A (en) * 2006-12-05 2008-06-19 Car Plaza Kumamoto:Kk Method for producing amino acid liquid from white distilled liquor lees, and amino acid liquid produced by this method
JP2009082764A (en) * 2007-09-27 2009-04-23 Jiro Toyoda Method of and apparatus for drying food garbage
JP2010183875A (en) * 2009-02-12 2010-08-26 Tech Corporation:Kk Method and apparatus for producing feed using squeezed residue of apple juice

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008136448A (en) * 2006-12-05 2008-06-19 Car Plaza Kumamoto:Kk Method for producing amino acid liquid from white distilled liquor lees, and amino acid liquid produced by this method
JP2009082764A (en) * 2007-09-27 2009-04-23 Jiro Toyoda Method of and apparatus for drying food garbage
JP2010183875A (en) * 2009-02-12 2010-08-26 Tech Corporation:Kk Method and apparatus for producing feed using squeezed residue of apple juice

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