JP2002112713A - Feed additive, and apparatus and method for producing the same - Google Patents

Feed additive, and apparatus and method for producing the same

Info

Publication number
JP2002112713A
JP2002112713A JP2000303638A JP2000303638A JP2002112713A JP 2002112713 A JP2002112713 A JP 2002112713A JP 2000303638 A JP2000303638 A JP 2000303638A JP 2000303638 A JP2000303638 A JP 2000303638A JP 2002112713 A JP2002112713 A JP 2002112713A
Authority
JP
Japan
Prior art keywords
radiation surface
surface temperature
far
animal feed
food
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
JP2000303638A
Other languages
Japanese (ja)
Inventor
Saburo Maruko
三郎 丸子
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 Chemical Plant Consultant Co Ltd
Original Assignee
Nippon Chemical Plant Consultant Co 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 Nippon Chemical Plant Consultant Co Ltd filed Critical Nippon Chemical Plant Consultant Co Ltd
Priority to JP2000303638A priority Critical patent/JP2002112713A/en
Publication of JP2002112713A publication Critical patent/JP2002112713A/en
Pending 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

Abstract

PROBLEM TO BE SOLVED: To provide a drying method involved in treating food residues and comprising bringing the water content of the residues to <=10 wt.% in a short time without causing scorching while putting the oxidative deterioration of the oily component of the residues to a minimum, and to provide a small-sized dryer enabling the method to be accomplished. SOLUTION: This drying method comprises the following process: food residues are finely cut or ground and then continuously irradiated with far- infrared rays with the main wavelengths of 4 μm (irradiated surface temperature of 450 deg.C) to 6.5 μm (irradiated surface temperature of 173 deg.C) while renewing the surface of the cut or ground food residues by an appropriate means.

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、レストラン等より
発生する食品残渣を動物飼料等として有効利用するため
の装置および方法、並びにそのような飼料等そのものに
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus and a method for effectively utilizing food residues generated from restaurants and the like as animal feed and the like, and to such feed and the like.

【0002】[0002]

【従来の技術】従来、レストランなどから発生する食品
残渣は、産業廃棄物として焼却するか、コンポストとし
て肥料にするかの方法しかなかった。しかしながら、焼
却を行えばダイオキシン等の発生の恐れが大きく、コン
ポストによる活用も、発生する食品残渣の季節変動や経
日変動のために、肥料として必ずしも適切であるとはい
えなかった。一方乾燥して再利用しようとすると、従来
の電気ヒーターなどによる方法では主波長が3.5μm
より短波長の赤外線を照射することになり、部分的に焦
げが生じ易くなり、飼料として有効な品質が得られなか
った。またスチームジャケット方式による乾燥では、ボ
イラーを別に設置しなければならず、また加熱面に乾燥
物が強固に付着することもあり、経済的にも構造的にも
問題があった。さらに熱風での乾燥では、熱風の入口温
度を300℃程度とし、出口温度は約100℃程度に抑
えねばならないので、エネルギーの利用効率は著しく悪
い上、悪臭発生という別の公害を招いていた。そのため
に、食品残渣の再利用については困難性があった。一
方、食品残渣はその中に炭水化物、タンパク質、油分、
水分等が色々な割合で混在するので、食品残渣が発生し
た場所で、直ちに水分を10%以下にしないと腐敗する
という性質のものであり、この点でも食品残渣の再利用
は難しいものであった。
2. Description of the Related Art Conventionally, food residues generated from restaurants and the like have only been incinerated as industrial waste or fertilized as compost. However, if incinerated, dioxin and the like are likely to be generated, and the use of compost is not always suitable as a fertilizer due to the seasonal variation and daily variation of the generated food residue. On the other hand, if it is to be dried and reused, the method using a conventional electric heater or the like has a main wavelength of 3.5 μm.
Irradiation with shorter-wavelength infrared rays was caused, and scorching was likely to occur partially, and effective quality as feed could not be obtained. Further, in the drying by the steam jacket method, a boiler must be separately installed, and the dried matter may be firmly adhered to the heated surface, which is economically and structurally problematic. Further, in the drying with hot air, the hot air inlet temperature must be set to about 300 ° C. and the outlet temperature must be suppressed to about 100 ° C., so that the energy use efficiency is remarkably poor and another pollution such as generation of offensive odor has been caused. For this reason, there was difficulty in reusing food residues. Food residues, on the other hand, contain carbohydrates, proteins, oils,
Since water and the like are mixed in various ratios, the food residue is apt to rot unless the water content is immediately reduced to 10% or less at the place where the food residue is generated. In this respect, it is difficult to reuse the food residue. Was.

【0003】[0003]

【発明が解決しようとする課題】本発明は、食品残渣の
再利用において従来の方法・装置ではなしえなかった油
分の酸化変質を最小限度にして、焦げを作ることなく短
時間で水分を10%以下にする乾燥方法と、それを達成
できる小型の装置を提供すると共に、このような方法及
び装置によって得られる飼料等を提供することを課題と
する。
The object of the present invention is to minimize the oxidative deterioration of oil which could not be achieved by the conventional method / apparatus in the recycling of food residues, and to reduce the amount of water in a short time without burning. %, And a small apparatus capable of achieving the drying method, and a feed obtained by such a method and apparatus.

【0004】[0004]

【課題を解決するための手段】食品残渣を細かく裁断又
は粉砕した後に、適宜の方法で表面更新させながら、主
波長4μm(放射面温度450℃)〜6.5μm(放射
面温度173℃)の遠赤外線を連続的に照射する。
After the food residue is finely cut or pulverized, the main wavelength is changed from 4 μm (radiation surface temperature of 450 ° C.) to 6.5 μm (radiation surface temperature of 173 ° C.) while the surface is renewed by an appropriate method. Irradiates far infrared rays continuously.

【0005】[0005]

【作 用】食品残渣を低温で、水分のみを蒸発し、油
分の酸化変質を防いで、短時間に経済的に乾燥できるの
で動物飼料添加物に適した材料が得られる。
[Action] Food residues can be dried at low temperature and only water evaporates to prevent oxidative deterioration of oil and can be economically dried in a short time. Therefore, a material suitable for animal feed additives can be obtained.

【0006】[0006]

【発明の実施の形態】本発明は、基本的には細分化した
食品を、撹拌機能と送り機能を有する装置上で遠赤外線
照射するものであるが、以下これらについて詳細に説明
する。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention is basically directed to irradiating far-infrared rays on a finely divided food on a device having a stirring function and a feeding function. These will be described in detail below.

【0007】食品残渣の前処理 食品残渣は、あらかじめ5mm程度、或いはそれより小
さい細片或いは細粉に粗く裁断又は粉砕してから、乾燥
装置に投入することが望ましい。また、食品残渣が油の
含有量が高い時には、あらかじめ食物繊維を構成成分と
する油吸収剤、例えば、おからを適当量添加することが
望ましい。
Pretreatment of Food Residue It is desirable that the food residue is roughly cut or crushed into small pieces or fine powder of about 5 mm or smaller in advance and then charged into a drying device. When the food residue has a high oil content, it is preferable to add an appropriate amount of an oil absorbent containing dietary fiber as a component, for example, okara.

【0008】乾燥 乾燥は、細分化された食品残渣の撹拌・送り機能を備え
た搬送装置と食品残渣に遠赤外線を照射する部分とを有
する装置でなされる。搬送装置は、複数の上方開放の半
円筒を水平に合わせ、それぞれの両端に内容物が他の半
円筒に移動しうる空間を設けた容器内に、各半円筒毎
に、互いに送り方向が逆の送り機能と撹拌機能を有し、
末端に隣接する半円筒に内容物を送り込む機能を有する
撹拌搬送からなる。送り機能と撹拌機能を有する具体的
手段としては例えば傾斜した羽根の回転による。一方の
半円筒から、他方の半円筒への食物残渣の移動は前記羽
根の横移動成分を増すような形状変化を利用する。食物
残渣は、上記のような撹拌搬送装置内で、含まれる水分
の量によっては、繰り返し搬送して乾燥処理を受けるよ
うにするが、並列される半円筒の数を増して内容物の搬
送経路自体を長くしても良い。熱源としては、主波長4
μm(放射面温度450℃)〜6.5μm(放射面温度
173℃)に調節できる遠赤外線を用いる。照射する遠
赤外線の波長は一定でも良いが、水分を多量に含んでい
る乾燥装置投入口に近い部分は、エネルギー密度の比較
的高い主波長の短めの遠赤外線を照射し、乾燥が進むに
つれて、主波長の長いエネルギー密度の低い遠赤外線を
放射するよう調節することも、短時間で焦げを極力少な
く乾燥する方法として有用であり、経済的である。
Drying Drying is performed by a device having a conveying device having a function of stirring and feeding the finely divided food residue and a portion for irradiating the food residue with far-infrared rays. The transport device aligns a plurality of half-cylinders opened upward horizontally, and in a container provided with a space at each end at which the contents can move to another half-cylinder, the feeding direction is reversed for each half-cylinder. With a feed function and a stirring function.
It consists of stirring and transporting, which has the function of feeding the contents into the half cylinder adjacent to the end. As a specific means having a feeding function and a stirring function, for example, rotation of an inclined blade is used. The movement of the food residue from one half cylinder to the other half cylinder utilizes a shape change that increases the lateral movement component of the blade. The food residue is repeatedly transported and subjected to the drying process in the above-described stirring and transporting device, depending on the amount of water contained therein, but the number of half cylinders arranged in parallel is increased to transport the contents. It may be longer. As the heat source, dominant wavelength 4
Far-infrared rays that can be adjusted to μm (radiation surface temperature: 450 ° C.) to 6.5 μm (radiation surface temperature: 173 ° C.) are used. The wavelength of the far-infrared ray to be irradiated may be constant, but the part near the drying device inlet, which contains a large amount of water, irradiates the shorter far-infrared ray of the main wavelength with a relatively high energy density, and as the drying proceeds, Adjustment to emit long-wavelength long-wavelength, low-energy-density far-infrared rays is also useful and economical as a method of drying in a short time with as little burning as possible.

【0009】処理 乾燥装置の一端に投入された食品残渣は、半円筒内に設
けら得た撹拌機能と送り機能を有する撹拌搬送装置で、
撹拌され表面更新をされながら、遠赤外線の照射を上方
から受けつつ、乾燥装置の他端(末端)にゆっくり輸送
される。撹拌搬送装置の末端は、隣接する半円筒内に内
容物を移送する作用を持つ羽根状の形状をしているの
で、部分乾燥された食品残渣はここで隣接半円筒に移動
し、その内部を今迄と逆方向に移動しながら乾燥され
る。この操作は、食品残渣に含まれる水分の量によって
繰り返しても良いし、設置面積にゆとりがあり、あらか
じめ水分量や処理量が多いと想定される場合には、並列
する半円筒の数を増やしておくことも有用である。本発
明の乾燥を用いて得られた乾燥物は、水分が少なく、容
易に10%以下にすることが可能であり、その成分とし
て動物の栄養となる炭水化物、タンパク質、油分、その
他の有用成分を含むから、従来公知の動物飼料に添加物
として混合した場合、栄養価を余り損なうことなく長期
保存に耐えるので、公害発生源としての食品残渣を有効
に利用する方法として、極めて有用である。公知の動物
飼料に混入する量に特に制限はないが、栄養のバラン
ス、バラツキなどを考慮すると、全体の20%程、或い
はそれより少なめに混合するのが望ましい。
[0009] The food residue introduced into one end of the drying device is agitated and conveyed with a stirring function and a feeding function provided in a half cylinder.
While being agitated and renewing the surface, it is slowly transported to the other end (end) of the drying device while receiving irradiation of far infrared rays from above. Since the end of the stirring and conveying device has a wing-like shape that has a function of transferring the contents into an adjacent half cylinder, the partially dried food residue moves to the adjacent half cylinder here, and the inside of the half is dried. It is dried while moving in the opposite direction. This operation may be repeated depending on the amount of water contained in the food residue, or if there is enough space in the installation area and it is assumed that the amount of water or the amount of treatment is large in advance, increase the number of parallel half cylinders. It is also useful to keep it. The dried product obtained by using the drying of the present invention has a low water content and can be easily reduced to 10% or less. As its components, carbohydrates, proteins, oils, and other useful components which are animal nutrition are contained. Therefore, when it is mixed with a conventionally known animal feed as an additive, it can withstand long-term storage without significantly impairing the nutritional value, and is extremely useful as a method for effectively utilizing food residues as a source of pollution. There is no particular limitation on the amount to be mixed into the known animal feed, but in consideration of nutritional balance, dispersion, etc., it is desirable to mix the mixture at about 20% or less of the whole.

【0010】[0010]

【実 施 例】本発明を使用した効率的な食品残渣の急
速乾燥方法並びに装置の一例を、図面に基づき説明す
る。食品残渣の投入口1より投入された食品残渣は、落
下した側の上方が開放した半円筒形外筒3内で、この半
円筒形外筒3に内蔵され長手方向回転軸2の半径方向外
側に配置された送り機能・撹拌機能を持つ羽根4によっ
て表面更新を受ながら、この半円筒形外筒3の一方の端
板6まで輸送される。この位置における前記長手方向回
転軸2の半径方向外側に配置された羽根4は食品残渣が
もはや半円筒外筒3の長手方向に向うのではなく、それ
と直角方向の横方向、即ち隣接する半円筒外筒3′方向
に移動するような構成とされている。一方、この端部位
置において両半円筒外筒3,3′はそれぞれ隣接する側
の筒部が取り去られているため、食品残渣は前記羽根4
によって、他方の半円筒外筒3′へ送り込まれる。この
他方の半円筒外筒3′内には、一方の半円筒外筒3の逆
方向に食品残渣を輸送するように全く同じ構成が用意さ
れており、食品残渣は輸送された後、前記端板6と反射
側の端板6′に至った後、前述した構成を備えていると
ころの、この端板6′に隣接する羽根5′および半円筒
外筒3,3′の隣接部の構造によって半円筒外筒3へと
輸送される。この間に、食品残渣は遠赤外線放射器10
から放射され、遠赤外線二次放射板11で調節された遠
赤外線により、上方から照射され、加熱される。加熱さ
れた内容物から蒸発した水分は乾燥装置排気口9から系
外に排出される。
EXAMPLE An example of an efficient method and apparatus for rapidly drying food residues using the present invention will be described with reference to the drawings. The food residue introduced from the food residue input port 1 is contained in the semi-cylindrical outer cylinder 3 inside the semi-cylindrical outer cylinder 3 having an open upper part on the side where the food residue is dropped, and is radially outside the longitudinal rotation shaft 2. The semi-cylindrical outer cylinder 3 is transported to one end plate 6 while receiving surface renewal by the blades 4 having a feeding function and a stirring function arranged in the outer cylinder 3. In this position, the blades 4 arranged radially outward of the longitudinal rotation axis 2 are such that the food residues are no longer directed in the longitudinal direction of the semi-cylindrical outer cylinder 3 but in a transverse direction perpendicular thereto, ie the adjacent semi-cylindrical cylinder. It is configured to move in the direction of the outer cylinder 3 '. On the other hand, at this end position, the two semi-cylindrical outer cylinders 3 and 3 'have their adjacent cylindrical parts removed, so that the food residue cannot
Is fed into the other half cylindrical outer cylinder 3 '. In the other half-cylindrical outer cylinder 3 ′, exactly the same configuration is provided so as to transport the food residue in the opposite direction of the one half-cylindrical outer cylinder 3. After reaching the plate 6 and the end plate 6 'on the reflection side, the structure of the blade 5' adjacent to the end plate 6 'and the adjacent portion of the semi-cylindrical outer cylinders 3, 3' having the above-mentioned structure. Is transported to the semi-cylindrical outer cylinder 3. During this time, the food residue is transferred to the far-infrared radiator 10
Irradiates from above with the far infrared rays adjusted by the far infrared secondary radiating plate 11 and is heated. Moisture evaporated from the heated contents is discharged out of the system through a drying device exhaust port 9.

【0011】図面に示した遠赤外線放射器10は、ステ
ンレスパイプの表面に遠赤外線放射塗料をコーティング
したもので、内部にニクロム線の発熱体を内蔵してい
る。表面温度は550℃で、主波長は3.5μmとなっ
ている。この放射器から放射される遠赤外線を直接食品
残渣に照射すると、撹拌を十分行い表面更新を活発にし
たとしても、乾燥生成物に部分的に焦げを生成する。従
って、表面積を広くした二次放射面を設置して、放射器
からの直接の遠赤外線をこの裏面に受け、反対側の表面
から、主波長の長いエネルギー密度の低い遠赤外線を遠
赤外線二次放射板11から二次放射させ、これで食品残
渣を照射すれば、焦げを生じることなく乾燥が行え、目
的を達成することができる。乾燥の終了は、半円筒形乾
燥装置外筒3又は3′の端板5又は6の近傍で、乾燥物
が隣接筒に移動する際に、乾燥生成物の温度を測定する
ことにより判断することができる。乾燥が終了したこと
を例えばマイコンが判断した時は自動もしくは手動によ
り、半円筒外筒3,3のいずれかの任意の箇所の底部に
用意された取出口13の蓋14が下方向に回動されるこ
とによって下方に用意された乾燥物受入タンク14中に
順次乾燥した食品残渣が回収される。この蓋の開閉方法
については、横回動、横移動等であっても良い。処理量
が多い場合には、半円筒を多数隣接させた乾燥装置を使
用することにより、循環させずワンパスで乾燥する方法
も使用できる。前述したように、この乾燥装置である程
度部分乾燥した後、乾燥物を一旦系外に取り出し、1〜
2mm位の細粒に粉砕し、再び乾燥装置に戻して乾燥を
行えば乾燥時間を短縮することも可能である。
The far-infrared radiator 10 shown in the drawing is a stainless steel pipe whose surface is coated with far-infrared radiation paint, and has a built-in heating element of nichrome wire inside. The surface temperature is 550 ° C., and the dominant wavelength is 3.5 μm. When far-infrared rays emitted from this radiator are directly radiated to food residues, even if the stirring is sufficient and the surface renewal is activated, the dried product partially burns. Therefore, a secondary radiating surface with a large surface area is installed to receive direct far-infrared rays from the radiator on this back surface, and from the opposite surface, far-infrared rays with a long dominant wavelength and low energy density If secondary radiation is emitted from the radiation plate 11 and the food residue is irradiated with the secondary radiation, drying can be performed without burning and the object can be achieved. The end of the drying should be determined by measuring the temperature of the dried product when the dried product moves to the adjacent tube near the end plate 5 or 6 of the semi-cylindrical drying device outer tube 3 or 3 '. Can be. When the microcomputer determines that the drying is completed, for example, the lid 14 of the outlet 13 provided at the bottom of any one of the semi-cylindrical outer cylinders 3 is automatically or manually rotated downward. As a result, sequentially dried food residues are collected in the dried product receiving tank 14 prepared below. The method of opening and closing the lid may be lateral rotation, lateral movement, or the like. When the throughput is large, a method of drying in a single pass without circulation may be used by using a drying device having a large number of half cylinders adjacent to each other. As described above, after partially drying to some extent with this drying apparatus, the dried product is once taken out of the system, and
It is also possible to shorten the drying time by crushing into fine particles of about 2 mm and returning to the drying device again for drying.

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

【図1】撹拌装置の正面側の要素を取り去って内部を見
せている、本発明による乾燥装置の正面図である。
FIG. 1 is a front view of a drying apparatus according to the present invention, with the front side elements of the stirring apparatus removed to show the interior.

【図2】撹拌装置の上面側の要素を取り去って内部を見
せている、図1の装置の上面図である(但し、取出口1
3は半円筒外筒3側にある例としている)。
FIG. 2 is a top view of the apparatus of FIG. 1 in which elements on the upper side of the stirring apparatus have been removed to show the inside thereof (excluding an outlet 1).
3 is an example on the side of the semi-cylindrical outer cylinder 3).

【図3】撹拌部において撹拌機構を取り去って、遠赤外
線装置、投入口、排出口の関係のみを示している図1の
装置の上面図である。
FIG. 3 is a top view of the apparatus of FIG. 1 with the stirring mechanism removed from the stirring section and showing only the relationship between the far-infrared ray device, the inlet, and the outlet.

【図4】図1の装置の矢印方向のA−A断面図である。FIG. 4 is a sectional view of the device of FIG.

【符号の説明】[Explanation of symbols]

1…食品残渣投入口、2,2′…回転軸、3,3′…半
円筒形外筒、4,4′…半径方向外側に配置された羽
根、6,6′…端板、9…排気口、10…遠赤外線放射
器、11…遠赤外線二次放射板、12…撹拌装置駆動用
ギア、13…取出口、14…蓋、15…乾燥物受入タン
1 ... food residue inlet, 2, 2 '... rotating shaft, 3, 3' ... semi-cylindrical outer cylinder, 4, 4 '... blades arranged radially outside, 6, 6' ... end plate, 9 ... Exhaust port, 10: Far-infrared radiator, 11: Far-infrared secondary radiating plate, 12: Gear for driving the stirrer, 13: Outlet, 14: Lid, 15: Dry matter receiving tank

フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) B09B 5/00 ZAB F26B 9/06 Q F26B 3/30 17/20 C 9/06 B09B 3/00 Z 17/20 303M 5/00 ZABP Fターム(参考) 2B150 BA04 BD05 BD06 BE01 BE02 CD37 3L113 AA06 AA08 AB06 AC10 AC35 AC45 AC46 AC58 AC63 BA01 CB06 CB22 CB29 DA10 DA14 DA24 4D004 AA04 BA04 CA04 CA07 CA42 CA43 CB13 DA02 DA03 DA06 4G066 AC06A AC06B AC07B BA16 CA05 DA07 DA09 FA21 FA31 FA34 FA37 4G075 AA37 CA02 CA35 Continuation of the front page (51) Int.Cl. 7 Identification symbol FI Theme coat II (reference) B09B 5/00 ZAB F26B 9/06 Q F26B 3/30 17/20 C 9/06 B09B 3/00 Z 17/20 303M 5/00 ZABP F term (reference) 2B150 BA04 BD05 BD06 BE01 BE02 CD37 3L113 AA06 AA08 AB06 AC10 AC35 AC45 AC46 AC58 AC63 BA01 CB06 CB22 CB29 DA10 DA14 DA24 4D004 AA04 BA04 CA04 CA07 CA42 CA43 CB13 DA02 DA06 DA06 AC06 AC06 DA07 DA09 FA21 FA31 FA34 FA37 4G075 AA37 CA02 CA35

Claims (12)

【特許請求の範囲】[Claims] 【請求項1】 食品残渣を細かく裁断又は粉砕した後
に、適宜の方法で表面更新させながら、主波長4μm
(放射面温度450℃)〜6.5μm(放射面温度17
3℃)の遠赤外線を、連続的に照射して得られた水分の
少ない食品再利用動物飼料添加物。
1. After the food residue is finely cut or pulverized, the main wavelength is 4 μm while the surface is renewed by an appropriate method.
(Radiation surface temperature 450 ° C.) to 6.5 μm (radiation surface temperature 17
(3 ° C.), a low water content food reuse animal feed additive obtained by continuously irradiating far infrared rays.
【請求項2】 請求項1記載の飼料添加物を従来公知の
動物用飼料に混合して得られる動物用飼料。
2. An animal feed obtained by mixing the feed additive according to claim 1 with a conventionally known animal feed.
【請求項3】 金属、ガラス等の自然分解しにくい混入
雑物等を除去した食品残渣を細かく裁断又は粉砕した後
に、適宜の方法で表面更新させながら、主波長4μm
(放射面温度450℃)〜6.5μm(放射面温度17
3℃)の遠赤外線を、食品残渣が焦げない程度の距離か
ら連続的に照射し、焦げを作らないように乾燥すること
を特徴とする、食品を再利用した動物飼料添加物の製造
方法。
3. After finely cutting or pulverizing a food residue from which contaminants such as metal and glass which are hardly naturally decomposed are removed, and renewing the surface by an appropriate method, the main wavelength is 4 μm.
(Radiation surface temperature 450 ° C.) to 6.5 μm (radiation surface temperature 17
A method for producing an animal feed additive that reuses food, characterized by continuously irradiating far infrared rays (3 ° C.) from a distance at which food residues do not burn and drying so as not to cause burning.
【請求項4】 食物繊維を構成成分とする油吸収剤を、
食品残渣の含有する油分に応じて乾燥に先立って適当量
添加することを特徴とする、請求項3記載の製造方法。
4. An oil absorbent comprising dietary fiber as a component,
4. The method according to claim 3, wherein an appropriate amount is added prior to drying depending on the oil content of the food residue.
【請求項5】 請求項3又は4記載の方法に従って乾燥
した乾燥生成物を、従来公知の動物用飼料に混合するこ
とを特徴とする、食品を再利用した動物飼料の製造方
法。
5. A method for producing an animal feed by reusing food, wherein the dried product dried according to the method of claim 3 or 4 is mixed with a conventionally known animal feed.
【請求項6】 乾燥生成物の水分10%以下のものを使
用することを特徴とする請求項5記載の食品を再利用し
た動物飼料の製造方法。
6. The method according to claim 5, wherein the dried product has a water content of 10% or less.
【請求項7】 主波長4μm(放射面温度450℃)〜
6.5μm(放射面温度173℃)の遠赤外線を、食品
残渣が焦げない程度の距離から連続的に照射し、得られ
た乾燥物を従来公知の動物飼料に20%を超えない程度
混合することを特徴とする請求項4,5および6の何れ
か1つに記載の動物飼料の製造方法。
7. Main wavelength: 4 μm (radiation surface temperature: 450 ° C.)
Far infrared rays of 6.5 μm (radiation surface temperature: 173 ° C.) are continuously irradiated from a distance such that the food residue does not burn, and the obtained dried product is mixed with a conventionally known animal feed so as not to exceed 20%. The method for producing an animal feed according to any one of claims 4, 5, and 6, wherein:
【請求項8】 遠赤外線放射装置から放射する遠赤外線
の波長を、主波長4μm(放射面温度450℃)〜6.
5μm(放射面温度173℃)に調節し、攪拌機能と搬
送機能を有する攪拌搬送装置を内蔵する乾燥装置の上方
から照射し、焦げを作ることなく内容物を乾燥すること
を特徴とする乾燥装置。
8. The wavelength of far-infrared rays emitted from the far-infrared ray radiating device is set to a main wavelength of 4 μm (radiation surface temperature of 450 ° C.) to 6.
A drying device characterized in that the content is adjusted to 5 μm (radiation surface temperature: 173 ° C.), irradiated from above a drying device having a stirring and conveying device having a stirring function and a conveying function, and the contents are dried without burning. .
【請求項9】 複数の半円筒を水平に合わせ、それぞれ
の両端に内容物が他の半円筒に移動しうる空間を設けた
容器内に、各半円筒毎に互いに送り方向が逆の送り機能
と撹拌機能を有し、末端に隣接する半円筒に内容物を送
り込む機能を有する撹拌搬送装置を内蔵設置したことを
特徴とする請求項8記載の乾燥装置。
9. A feeding function in which a plurality of half-cylinders are horizontally aligned, and a feeding direction is reversed for each half-cylinder in a container provided with a space at each end at which contents can move to another half-cylinder. 9. The drying apparatus according to claim 8, further comprising a built-in stirring / conveying apparatus having a function of feeding the contents into a half cylinder adjacent to the end and a function of stirring.
【請求項10】 主波長4μm(放射面温度450℃)
〜6.5μm(放射面温度173℃)に調節できる遠赤
外線の放射面を得るために、小面積の一次放射面を有す
る放射体を内蔵し、大面積の二次放射面を残し他の部分
は保温した放射器から、主波長4μm(放射面温度45
0℃)〜6.5μm(放射面温度173℃)の遠赤外線
を放射することを特徴とする請求項8又は9に記載の乾
燥装置。
10. Main wavelength: 4 μm (radiation surface temperature: 450 ° C.)
In order to obtain a far-infrared radiation surface that can be adjusted to ~ 6.5 µm (radiation surface temperature: 173 ° C), a radiator with a small-area primary radiation surface is built in, and other parts except a large-area secondary radiation surface Is a main wavelength of 4 μm (radiation surface temperature of 45 μm)
The drying device according to claim 8, wherein the drying device emits far infrared rays having a temperature of 0 ° C.) to 6.5 μm (radiation surface temperature: 173 ° C.).
【請求項11】 食品残渣を供給する投入装置、裁断又
は粉砕する粉末化装置、細粉搬送装置に対面して設置さ
れた遠赤外線放射装置、細粉を混合撹拌しながら搬送す
る細粉搬送装置、必要に応じ適当な動物飼料を添加混合
する撹拌混合装置からなることと特徴とする食品再利用
動物飼料製造装置。
11. A feeding device for supplying a food residue, a powdering device for cutting or pulverizing, a far-infrared radiation device installed facing the fine powder conveying device, and a fine powder conveying device for conveying the fine powder while mixing and stirring. And a stirring and mixing device for adding and mixing an appropriate animal feed as needed.
【請求項12】 遠赤外線放射装置から放射する遠赤外
線の波長を、主波長4μm(放射面温度450℃)〜
6.5μm(放射面温度173℃)に調節することを特
徴とする請求項11記載の食品再利用動物飼料製造装
置。
12. The wavelength of far-infrared rays emitted from the far-infrared ray radiating device is set to a main wavelength of 4 μm (radiation surface temperature of 450 ° C.).
The animal feed producing apparatus according to claim 11, wherein the apparatus is adjusted to 6.5 µm (radiation surface temperature: 173 ° C).
JP2000303638A 2000-10-03 2000-10-03 Feed additive, and apparatus and method for producing the same Pending JP2002112713A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000303638A JP2002112713A (en) 2000-10-03 2000-10-03 Feed additive, and apparatus and method for producing the same

Publications (1)

Publication Number Publication Date
JP2002112713A true JP2002112713A (en) 2002-04-16

Family

ID=18784815

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2002112713A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006226549A (en) * 2005-02-15 2006-08-31 Nippo Corporation:Kk Particulate heating device
JP2016136892A (en) * 2015-01-28 2016-08-04 北越電建株式会社 Livestock feed manufacturing system
CN108981371A (en) * 2018-08-26 2018-12-11 徐亮 A kind of multi-functional agricultural seed drying device

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JPH02186949A (en) * 1989-01-13 1990-07-23 Zenoosaka Sakana Tanpaku Jigiyou Kyodo Kumiai Bait for fish culture and production thereof
JPH07195058A (en) * 1993-11-26 1995-08-01 Chubu Drum Kan Kogyo Kk Treatment of crude refuse and the like and treating device for crude refuse and the like
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Publication number Priority date Publication date Assignee Title
JP2006226549A (en) * 2005-02-15 2006-08-31 Nippo Corporation:Kk Particulate heating device
JP2016136892A (en) * 2015-01-28 2016-08-04 北越電建株式会社 Livestock feed manufacturing system
CN108981371A (en) * 2018-08-26 2018-12-11 徐亮 A kind of multi-functional agricultural seed drying device

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