JP4117521B2 - Horizontal rotary cylindrical continuous stirrer with exhaust hot air introduction type - Google Patents

Horizontal rotary cylindrical continuous stirrer with exhaust hot air introduction type Download PDF

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Publication number
JP4117521B2
JP4117521B2 JP2000307369A JP2000307369A JP4117521B2 JP 4117521 B2 JP4117521 B2 JP 4117521B2 JP 2000307369 A JP2000307369 A JP 2000307369A JP 2000307369 A JP2000307369 A JP 2000307369A JP 4117521 B2 JP4117521 B2 JP 4117521B2
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Prior art keywords
hot air
cylinder
exhaust
horizontal
fried
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JP2000307369A
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JP2002112896A (en
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貞二郎 中村
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Ajinomoto Co Inc
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Ajinomoto Co Inc
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Description

【0001】
【発明の属する技術分野】
本発明は、焼きそば、焼飯、ピラフ、スクランブルエッグ、キンピラゴボウ、野菜炒めなどの炒め食品、および炒めタマネギ、ソフリット、肉、魚介類などの前処理としての炒め調理を連続的かつ効率的に行う炒め装置に関する。
【0002】
【従来技術】
従来、炒め食品および食品製造の前処理としていた炒めを行う装置としては、(1)攪拌機付きの平釜式炒め機、(2)回分式のロータリー式炒め機、(3)回分式ロータリー炒め機において丸底の中央部に排熱風吹き出し口を設けたものおよび(4)横型回転円筒の内面に突起物をスパイラル状に配列したロータリー式の連続炒め機が知られている。
【0003】
(1)攪拌機付きの平釜式炒め機は、従来から最も多く使われてきた炒め機であり、鍋の底面をガス焚きし炒め材料を攪拌機で混合する方式のものであるが、釜の容積に見合った量の炒め材料しか張り込むことが出来ない。もし一度に多く張り込むと釜の温度が急激に下がってしまい、温度回復には時間が掛り、その間に炒め材料特に水分の多い野菜から水分が滲出し、それが多量に釜底に残り、煮込みのような状態になってしまうことがある。
【0004】
すなわち、回分式炒め機においては、炒め材料の張り込み時に釜温度が急激に下がるため一度に多く張り込めず1台当たりの生産能力が低く、また炒め材料の出し入れに人手を要する。また、回分式においては処理開始時と終了時では熱負荷が大きく変わるため、人が付いて壁面の温度管理をしなくてはならない。また開口部が大きく、その分フードの排気量も大きくなり、空調負荷も大となる。大量生産するためには多数の釜を並べざるを得ず、そのための設置スペースが多く要する。
【0005】
(2)回分式のロータリー炒め釜は、丸底で上部が開放され、内壁に1〜2枚程度の掻き上げ羽根が付いた円筒を、材料がこぼれないように斜めに保った状態で回転させ、材料を掻き上げ、落下、分散、混合を繰り返しながら、外周部をガス焚き加熱する方式のものであるが、(1)と同様に回分式であるための欠点を持っている。
【0006】
(3)ロータリードラムの底部に燃焼ガス又は燃焼ガスによって間接加熱された熱風の吹き出し口を設けた回分式ロータリー炒め機については実開昭62−83323号公報に記載されているように、上記(2)ロータリー炒め機に比べてエネルギー効率・処理品質面で改善されてはいるが、やはり前記した回分式の欠点を持ち合わせている。また処理初期時と終了時では熱負荷が大きく変わるため熱風の温度制御が困難であるという問題がある。
【0007】
(4)食品連続炒め機は特開平6−189855号公報によって提案されているように、円筒状のドラムを傾斜状に配設して上方開口部に投入口を下方開口部に吐出口を設け、銅部内周面に突起物を螺旋状に配して、ドラムを回転させ、外周面を加熱し、連続的に調理する炒め器であって、回分式の欠点は解消されているものの、処理材料への熱伝達は円筒内壁面だけに頼っており、内壁面積当たりの熱負荷が大きくその分焦げ付きも当然多くなり長時間の連続運転には問題が残る。また構造的に円筒内に蒸気がこもりやすく、材料の水分が蒸発しにくい状態にあり蒸発能力と処理品の品質面に問題がある。
【0008】
【発明が解決しようとする課題】
本発明は、前記した従来の回分式炒め機及び連続炒め機の欠点を改善すべく、横型回転円筒式連続炒め機の中に燃焼排熱風を導入することによって、処理速度の向上、大量連続長時間運転の達成、エネルギー効率の向上、炒め品の品質の向上、省人、省スペースの達成を図ろうとするものである。
【0009】
【課題を解決するための手段】
本発明者らは上記従来技術・装置の問題点を解決すべく鋭意検討を行った結果、横型回転円筒式連続炒め機の中に、排熱風バイパスラインへの逃がし量及びフレッシュ空気の導入量を調整する調整手段(ダンパー)により温度及び風量が広範囲に変えられる燃焼排熱風を導入することにより、従来法の釜の壁面との接触伝熱に加えて、熱風による強制対流伝熱効果が得られ、炒め材料の速やかな昇温と、蒸発・乾燥が加速され、更に円筒内壁には掻き上げ羽根を取りつけ、掻き上げられた材料が落下する位置に合わせて、ほぐし用格子を取りつけることにより、ご飯物などのように回転・混合・移送中に団子状になりやすい材料を炒める場合でも、団子状にならずに炒めることができることを見いだし、本発明を完成するに至った。本発明によれば、熱風と炒め材料とは逆向きの流れ、いわゆる向流接触させることによって、その効果は一段と促進される。また円筒内壁の接触伝熱だけに頼らないため、壁面積当たりの熱負荷が減少でき壁面への焦げ付き度合も大幅に減少し、長時間の大量連続運転が可能である。更に又、この高効率・高能力の炒め機を使用し、連続大量生産することによって大幅な省人と省スペースも達成できる。また排熱風の熱エネルギーを有効利用することによる燃料の消費量を減少することができ、また開口部の極小化によってフードによる局所排気量が減少するため空調負荷の低減もでき、結果として大幅な省エネルギー化が達成できる。品質面においても熱風効果により処理品の水分を短時間で効率良く飛ばすことができ、ドリップに漬かることなく、また、ご飯物などのように回転・混合・移送中に団子状になりやすい材料を炒める場合でも、団子状にならずに良質な炒め品を得ることができる。本装置の運転条件の可変性については、1)横型円筒の回転数と傾斜角度を変えることによって自由な炒め時間が設定可能、2)円筒の壁面温度はガスの燃焼量によって変えることができる、3)必要によっては横方向の領域ごとに内壁面の温度帯を変えることができる、4)円筒内に導入する熱風の温度と風量は調整手段のバイバスへの熱風逃がし量及びフレッシュ空気の導入量によって広範囲に変えることができる。これらの1)〜4)による広範囲の運転条件の選択により、その材料に合った、その処理流量に合わせた或いは焦げ付き度合いに合わせたいわゆる多用な運転が可能な装置である。
【0010】
すなわち、本請求項1に係わる発明は、横型回転円筒式の連続炒め装置において、円筒の外周面の加熱に用いた燃焼ガスの排熱風を円筒内に導入する排熱風供給ラインを配設すると共に、回転円筒内部に導く排熱風を炒め材料の移送方向と逆向きとし、炒め材料と排熱風を向流接触せしめるように、排熱風供給ラインを炒め処理食品排出端側に連接し、該円筒内壁には掻き上げ羽根を取りつけ、掻き上げられた材料が落下する位置に合わせて、ほぐし用格子を取りつけたことを特徴とする排熱風導入型の横型回転円筒式連続炒め装置であり、加熱に用いた燃焼ガスの排熱風を処理材料と直接向流接触させ、強制対流効果を発揮させることによって、いわゆる並流接触に比べ炒め材料の昇温と蒸発を大幅に加速し、処理能力の向上、ドリップ(炒め材料からの水分の滲出)の出ない炒めによる品質の向上、円筒内壁への焦げ付き低減による長時間連続運転化を可能となる上に、ご飯物などのように団子状になりやすい材料を炒める場合でも、回転・混合・移送中に団子状にならずに炒めることが可能となり、合わせて熱効率の向上及び省人、省スペースの達成を図るものである。
【0012】
請求項に係わる発明は、排熱風供給ラインは、排熱風バイパスラインへの逃がし量及びフレッシュ空気導入量をそれぞれ調整するダンパーに接続しており、それぞれの開度に応じて円筒内部に導入する熱風の温度と風量を設定することを特徴とする請求項1記載の排熱風導入型の横型円筒回転式連続炒め装置であり、導入する排熱風は排熱風のバイパスラインへの逃がし量及びフレッシュ空気の導入量を調整する調整手段いわゆるダンパーの開度により、円筒内を通過する熱風の温度及び風量を広範囲に変えることができる。
【0013】
請求項に係わる発明は、横型回転円筒の横方向有効長と円筒内径の比が3以上であって、横型回転円筒の直下において外周面を加熱させる燃焼調整手段を付加した加熱手段を円筒の横方向に3区分以上にした領域ごとに個別に設けてあり、それぞれの領域ごとに燃焼負荷を調整して円筒内壁面の温度帯を個別に設定することを特徴とする請求項1記載の排熱風導入型の横型回転円筒式連続炒め装置であり、いわゆる十分に横方向に長い回転円筒においては熱伝導の性質上、内壁温は直近の外壁のガス燃焼量にある程度見合った温度帯になり、領域ごとに燃焼量を変えればそれぞれ違った温度帯を設定することができる。例えば、後記実施例の図1に示す領域Iでは強火で内壁の平均温度は230℃、領域IIでは弱火で190℃、領域IIIでは中火で210℃というように、その材料に合わせた、または焦げ付きを低減できる温度帯に合わせた幅広い温度領域の選択が可能である。
【0014】
【発明の実施の形態】
以下、図1及び図2を参照して本発明の排熱風導入型横型回転円筒式連続炒め機に係わる装置的な具備条件について説明する。図1は本発明の一実施例に係る排熱風導入型横型回転円筒式連続炒め機の構成図を示し、図2は該連続炒め機の一部を断面した側面図を示す。
【0015】
横型円筒5としては局部的な焦げ付き防止とムラのない平均的な加熱を行なうための十分な肉厚と十分な熱伝導性を有した金属材質(例えば、鉄鋼材料、銅系材料、ステンレス鋼等)を用いることが好ましく、また円筒内面は洗浄性及び焦げ付き防止を考慮して、出来るだけ鏡面仕上げとすることが好ましく、又はより長時間の連続運転を可能にするためにテフロンコーティング、テフロン含浸処理、金属粉末の溶射処理等の表面処理施工は有効な方法である。
【0016】
円筒内壁には処理材料を掻き上げるための高さ3〜15cm程度の掻き上げ羽根6を横方向に2段以上、円周方向に1枚以上取りつける。必要により掻き上げ羽根6には材料を排出側に送るための角度をつけることもあり、また羽根角度を変更できるような固定の仕方もある。またご飯物などのように回転・混合・移送中に団子状になりやすい材料を炒める場合は、実施例の図2に示すように落下する位置に合わせて、ほぐし用格子7を取りつける。
【0017】
円筒は排出側に向かってやや下がり勾配(1/20〜50)になるよう設置し(但し、掻き上げ羽根6に材料の送り角度を設けた場合はこの限りではない)、可変速の駆動装置9により回転される。処理材料の円筒内での滞留時間、いわゆる炒め時間は円筒の傾斜角度と回転数によって変えられる。
【0018】
連続運転の効率性を考慮して円筒の横方向長さと内径との比は3以上とするのが好ましい。
【0019】
回転円筒の外周部、主として底部周辺には、横方向に3基以上、円周方向には1〜3基の燃焼調整の出来るガスバーナーを配置し、いわゆる複数のバーナーを使用することによって小刻みに熱負荷調整を可能にする。
【0020】
また、ガス供給配管は実施例の図1のように円筒の横方向の領域ごとに区分し、区分ごとにガス燃焼調整弁またはこれに代わる手段を設けた方が好ましい。
【0021】
回転円筒の外壁には複数個の放射温度計11又はこれに代わる温度測定手段を配し、外壁温度の温度管理と監視を行なう。
【0022】
回転円筒の周囲には実施例の図2のように断熱材を兼ねた熱風カバー16を配し、円筒外壁とカバーとの間の流路を燃焼ガスが上昇し、頂上付近でダクト17に接続される。ダクト17は次に熱風バイパスライン19と分岐された後、煙塵除去フィルター21に入り、次にフレッシュ空気と一緒になり、円筒の処理品排出端側より円筒内に導入されるように排熱風供給ラインAが配設されている。尚、分岐の位置、フィルターの位置、フレッシュ空気導入の位置は、その順序にそれほどこだわるものではない。
【0023】
熱風バイパスライン19及びフレッシュ空気導入口にはそれぞれ流量調整用のダンパー20,22又はこれに代わる手段のものを配し、これの調整により円筒に導入する熱風の温度及び風量を設定する。
【0024】
連続式において熱風を導入することは今までになく、回分式のような材料の品温の上昇によって水分蒸発量が異なる系とは異なり、安定的に水分を制御することができるので、品質のムラも少なくすることが可能となった。
【0025】
材料投入端側から出る排風は、熱風バイパスライン19と一緒になった後排ガス清浄器25に入り、排風ファン26を経て大気放出される。
【0026】
一連の熱風ラインには3〜5個の温度計18を配置し、熱風の温度管理と監視を行なう。
【0027】
処理するための材料は原料投入シュート4又はこれに代わるスクリューフィーダーなどの投入手段を経て回転円筒内に供給される。
【0028】
材料は掻き上げ羽根6によって掻き上げられ、落下し、分散し、内壁と接触し、混合し、これを繰り返しながら、また熱風と強制対流接触しながら排出側へと進む。
【0029】
処理品は処理品排出シュート8又はこれに代わる手段を経て排出される。
【0030】
炒め調理に食油を使用する場合は油注入ポンプ3又はこれに代わる手段によって円筒内に供給される。
【0031】
円筒の処理品排出端側には前面扉23を配設しておき、円筒内洗浄時及び点検時には開放して行なう。
【0032】
横型回転円筒5、駆動装置9、燃焼用のガスバーナー12、断熱カバー16、熱風バイパス用ダンパー20、フレッシュ空気用ダンパー22、熱風バイパスライン19、原料投入シュート4、処理品排出シュート8、前面扉23、排風用フード24、温度計11、18等は出来るだけ同一の架台に設置することが好ましく、これによって回転円筒の傾斜角度を変更するときは架台の傾斜角を変更するだけでよく、架台に搭載されている上記の付属設備についてはそのままでよいことになる。
【0033】
架台の傾斜角度を容易に変更できる手段、例えばジャッキ28あるいはハンドル付きのネジ等を具備しておけばなお好ましい。
【0034】
また、長時間連続運転後の円筒内壁の焦げ付き落としについては、圧力10〜20メガパスカル程度のプランジャーポンプを発生源とした高圧水を用い、ジェットガンに接続し、円筒を回転させながらそのジェットガンを連続送り装置に取りつけて壁面に噴射すれば、ほとんど人手が掛らずに、きれいに洗浄できる。
【0035】
【実施例】
本発明を実施例に示した図面に基づいて具体的に説明するが、前項で説明した装置の具備条件等の一部は省略する。尚、本発明はこれに限定されるものではない。
【0036】
処理する各種材料は使用する食用油と共に原料定量供給機1にて混合されて、定量的に原料投入シュート4に投入される。一方食用油は給油タンク2より給油ポンプ3にて定量供給機1または食用油供給ラインから直接的に投入シュート4に供給される。材料及び食用油は次に横型回転円筒5の原料投入端側に入る。
【0037】
予め所定温度に加熱された回転円筒5に入った材料は掻き上げ羽根6により掻き上げられ、落下・分散・缶内壁との接触・混合を満遍なく繰り返しながら処理品排出端側へと進む。材料の滞留時間は円筒の傾斜角度と円筒の回転数によって決められる。
【0038】
ご飯物のように進行中に団子になりやすい物を処理する場合は、ほぐし用格子7を材料の落下する位置に取りつける。
【0039】
回転円筒内を進行中の材料は処理品排出端側から導入された熱風と常に直接的に接触され、いわゆる向流の強制対流伝熱が行なわれる。この強制対流伝熱により材料の昇温と水分の蒸発が効率良く促進される。
【0040】
円筒内を進行中の材料は熱風効果によりドリップにほとんど漬かることなく炒められ、いわゆる良質な炒め品ができることになる。
【0041】
排出端側より排出された処理品は処理品排出シュート8を経て処理品搬送コンベアーなどにより所定の場所に運搬される。
【0042】
回転円筒5は変速の可能な駆動装置を用い、また円筒への伝導は駆動歯車9によって行なわれ、片方側には受け用の回転ローラー10を設置している。
また回転円筒5は処理品の排出側に向かって若干の下がり勾配を有している。
【0043】
回転円筒の外周部、主として底部周辺には横方向に3基以上の複数基のガスバーナー12が配置され、このガスバーナーにより回転円筒5は加熱される。
【0044】
横方向に複数に配置したガスバーナー12の燃料供給配管は横方向に3つの領域に区分され、その区分ごとに燃焼調整弁13を設けている。この調整弁13により領域ごとに円筒内壁の温度帯を変えられることになる。これによってその材料に最も適した横方向の温度領域で運転することが出来る。
【0045】
ガスバーナー12の周辺には燃焼用給気口14及び燃焼状態点検口15を配設している。
【0046】
ガスバーナー12の燃焼ガスは断熱カバー16と円筒5の外壁との間の流路を通り、またこの間に円筒に熱を与えながら頂上部に上昇し、ダクト17に接続される。
【0047】
次に熱風は熱風バイパスライン19と分岐され煙塵除去フィルターに入り、すすが除去される。
熱風バイパスライン19には流量調整用のダンパー20を配設している。
【0048】
煙塵除去フィルター21を出た熱風は次にフレッシュ空気と混合され回転円筒の処理品排出端側へ導入される。フレッシュ空気はダンパー22によって風量が調整される。
【0049】
回転円筒に導入される熱風の温度と風量は熱風バイパスラインへの逃がし量(ダンパー20の開度による)とフレッシュ空気導入量(ダンパー22の開度による)によって、広範囲に設定出来る。
【0050】
円筒内に導入された熱風は、材料と強制対流伝熱をしながら、材料投入端側へと進み、排風用フード24に集口し、次に熱風バイパスライン19と合流した後、排ガス清浄噐25へと進む。
【0051】
湿式の排ガス清浄噐25では油煙が除去され、また水分が加えられ、排気ファン26へ吸引されて大気放出される。
【0052】
円筒の外壁温度測定用には放射温度計11を数個及び熱風の温度計18を数個取り付けて温度管理、監視を行なう。
【0053】
本装置は材料の熱変性度・水分量・焦げ付きやすさなどの性質に合わせ、また処理流量に合わせ回転数、対流時間、燃焼負荷量、円筒内壁の温度、円筒内壁の横方向の領域温度帯、熱風の温度と風量等をそれぞれ自由に変えられる仕組みになっており、幅広い運転が可能である。
【0054】
処理品排出側には円筒内洗浄時や点検時に使用する前面扉23を配設している。
【0055】
一方主架台27には横型回転円筒5とその関連装置の駆動装置、ガス燃焼装置、熱風装置等を搭載し、円筒の傾斜角度調整は角度調整用ジャッキ28によって行なう。
【0056】
【発明の効果】
本発明により、横型の回転円筒式連続炒め機を用い、ガス燃焼における排熱風を円筒内に導入し、処理品と向流の強制対流接触させることによって、材料の昇温と蒸発が大幅に促進され、処理能力の大幅向上、ほとんどドリップに漬かることのない良質な炒め、焦げ付きの低減による長時間連続運転化、省エネルギー、省スペースが達成できた。該円筒内壁には掻き上げ羽根を取りつけ、掻き上げられた材料が落下する位置に合わせて、ほぐし用格子を取りつけたことによってご飯物などのように団子状になりやすい材料を炒める場合でも、回転・混合・移送中に団子状にならずに炒めることが可能となった。また、本装置は熱風の温度、風量及び円筒内壁の温度などを高範囲に変えられる仕組みになっており、処理材料の性質や処理流量に合わせた、幅広い運転が可能である。
【図面の簡単な説明】
【図1】 本発明の一実施例による連続炒め装置の構成を示す図面。
【図2】 連続炒め装置の一部を断面した側面図。
【符号の説明】
1…原料定量供給機
2…給油タンク
3…給油ポンプ
4…原料投入シュート
5…横型回転円筒
6…掻き上げ羽根
7…ほぐし用格子
8…処理品排出シュート
9…円筒駆動用歯車
10…回転ローラー
11…外壁用放射温度計
12…ガスバーナー
13…燃焼調整弁
14…燃焼用給気口
15…燃焼状態点検口
16…断熱カバー
17…ダクト
18…熱風用温度計
19…熱風バイパスライン
20…バイパス用ダンパー
21…煙塵除去フィルター
22…フレッシュ空気用ダンパー
23…前面扉
24…排風用フード
25…排ガス清浄噐
26…排気ファン
27…主架台
28…傾斜角度調整用ジャッキ
29…処理品搬送コンベアー
[0001]
BACKGROUND OF THE INVENTION
The present invention is a fried food that continuously and efficiently performs stir-cooking as a pretreatment of fried foods such as fried noodles, fried rice, pilaf, scrambled eggs, butterflyfish, stir-fried vegetables, and fried onion, sofrit, meat, seafood, etc. Relates to the device.
[0002]
[Prior art]
Conventionally, as a device for fried foods and food preparation as a pretreatment of food production, (1) a flat pot type stirrer with a stirrer, (2) a batch type rotary stirrer, and (3) a batch type rotary stirrer And (4) a rotary continuous frying machine in which protrusions are arranged in a spiral shape on the inner surface of a horizontal rotary cylinder.
[0003]
(1) The flat pot type stirrer with a stirrer is the most commonly used stirrer, and it is a type that stirs the bottom of the pan with gas and mixes the stir material with the stirrer. Only the amount of stir-fried ingredients can be applied. If a lot is applied at once, the temperature of the kettle will drop sharply, and it will take some time for the temperature to recover. It may become the state like this.
[0004]
That is, in a batch-type stirrer, the temperature of the kettle drops drastically when stir-fry material is put in, so that a large amount cannot be put at once and the production capacity per unit is low, and manpower is required to put in and out the stir-fry material. In batch mode, the heat load changes greatly at the start and end of processing, so the person must be attached to manage the temperature of the wall. In addition, the opening is large, the amount of exhaust of the hood is increased accordingly, and the air conditioning load is also increased. For mass production, a large number of pots must be arranged, and a large installation space is required.
[0005]
(2) A batch-type rotary stir-fry pot is rotated with a round bottom, open at the top, and a cylinder with one or two scraping blades on the inner wall held diagonally to prevent spilling. This is a system in which the outer peripheral portion is heated by gas-fired while repeating the material scraping, dropping, dispersion and mixing, but has the disadvantage of being batch-type like (1).
[0006]
(3) As described in Japanese Utility Model Laid-Open No. 62-83323, a batch-type rotary stirrer in which a blowout port for hot air indirectly heated by combustion gas or combustion gas is provided at the bottom of the rotary drum, 2) Although it is improved in terms of energy efficiency and processing quality compared to the rotary stirrer, it still has the drawbacks of the batch method described above. In addition, there is a problem that it is difficult to control the temperature of the hot air because the heat load changes greatly at the initial stage and at the end of the process.
[0007]
(4) As proposed in Japanese Patent Laid-Open No. 6-189855, the continuous food frying machine is provided with a cylindrical drum in an inclined shape, and an inlet is provided in the upper opening and a discharge opening is provided in the lower opening. , A stirrer that spirally arranges protrusions on the inner peripheral surface of the copper part, rotates the drum, heats the outer peripheral surface, and cooks continuously. Heat transfer to the material relies only on the inner wall surface of the cylinder, the heat load per inner wall area is large, and naturally there is a lot of charring, and there remains a problem for long-term continuous operation. In addition, it is structurally easy for vapor to accumulate in the cylinder, and the moisture of the material is difficult to evaporate, which causes problems in the evaporation capability and the quality of the processed product.
[0008]
[Problems to be solved by the invention]
In order to improve the disadvantages of the conventional batch stirrer and continuous stirrer described above, the present invention introduces combustion exhaust hot air into the horizontal rotary cylindrical continuous stirrer, thereby improving the processing speed and mass continuous length. It aims to achieve time operation, improve energy efficiency, improve the quality of stir-fried products, and save labor and space.
[0009]
[Means for Solving the Problems]
As a result of intensive studies to solve the problems of the above-described prior art and devices, the present inventors have determined the amount of escape to the exhaust hot air bypass line and the amount of fresh air introduced into the horizontal rotary cylindrical continuous stirrer. By introducing combustion exhaust hot air whose temperature and air volume can be varied over a wide range by adjusting means (damper), in addition to contact heat transfer with the wall surface of the conventional method, a forced convection heat transfer effect by hot air can be obtained. By quickly raising the temperature of the stir-fried material and evaporating / drying it , the scraper blades are attached to the inner wall of the cylinder, and the loosening lattice is attached to the position where the scraped material falls. even when fry dumpling shape tends material during rotation, mixing, transfer, such as objects, found Rukoto can fry without being bunching, thereby completing the present invention. According to the present invention, the effect is further promoted by bringing the hot air and the stir-fried material into opposite flow, that is, so-called countercurrent contact. In addition, since it does not rely only on contact heat transfer on the inner wall of the cylinder, the heat load per wall area can be reduced, the degree of scorching on the wall surface can be significantly reduced, and long-term continuous operation is possible. Furthermore, by using this high-efficiency and high-capacity stirrer and continuously mass-producing them, significant labor and space savings can be achieved. In addition, the fuel consumption can be reduced by effectively using the heat energy of the exhaust hot air, and the local exhaust amount by the hood can be reduced by minimizing the opening, so that the air conditioning load can be reduced. Energy saving can be achieved. In terms of quality, the hot air effect can efficiently remove moisture from the processed product in a short period of time, and it can be used in a drip-free material such as rice, which tends to form dumplings during rotation, mixing and transfer. Even when fried , a high-quality fried product can be obtained without forming a dumpling . Regarding the variability of the operating conditions of this apparatus, 1) a free stir time can be set by changing the rotational speed and inclination angle of the horizontal cylinder, and 2) the wall surface temperature of the cylinder can be changed by the amount of gas combustion. 3) If necessary, the temperature zone of the inner wall surface can be changed for each region in the lateral direction. 4) The temperature and the amount of hot air introduced into the cylinder are the amount of hot air released into the bypass of the adjusting means and the amount of fresh air introduced. Can be changed widely. By selecting a wide range of operating conditions according to these 1) to 4), it is a device capable of so-called versatile operation that matches the processing flow rate or suits the degree of burning.
[0010]
That is, in the invention according to claim 1, in the horizontal rotary cylindrical continuous stirrer, the exhaust hot air supply line for introducing the exhaust hot air of the combustion gas used for heating the outer peripheral surface of the cylinder into the cylinder is disposed . The exhaust hot air leading to the inside of the rotating cylinder is opposite to the transfer direction of the stir-fried material, and the exhaust hot air supply line is connected to the stir-processed food discharge end side so that the stir-fried material and the exhaust hot air are in countercurrent contact with each other. Is a horizontal rotary cylindrical continuous stirrer with a hot air introduction type, which is equipped with a lifting blade and a lattice for loosening according to the position where the scraped material falls. the exhaust hot air had combustion gases is processed material and direct flow contact, by exerting a forced convection effect, greatly accelerates the heating and evaporation of the comparison fried material to a so-called parallel flow contact, improving the processing capability, drip ( In addition to being able to improve the quality by stir-fry that does not cause moisture exudation from the cooking material, and to reduce the burning on the inner wall of the cylinder, it can be operated continuously for a long time. In addition, fried materials such as rice are fried Even in this case, it is possible to fry without rotating into a dumpling during rotation, mixing, and transfer, and at the same time, it is intended to improve thermal efficiency and save labor and space.
[0012]
In the invention according to claim 2 , the exhaust hot air supply line is connected to a damper for adjusting the escape amount to the exhaust hot air bypass line and the fresh air introduction amount, respectively, and is introduced into the cylinder according to the respective opening degrees. 2. The exhaust hot air introduction type horizontal cylindrical rotary continuous frying device according to claim 1, wherein the temperature and the air flow of the hot air are set, and the exhaust hot air to be introduced is discharged to the bypass line of the exhaust hot air and fresh air The temperature of the hot air passing through the inside of the cylinder and the air volume can be varied over a wide range by adjusting the so-called damper opening.
[0013]
In the invention according to claim 3 , the ratio of the horizontal effective length of the horizontal rotating cylinder to the inner diameter of the cylinder is 3 or more, and the heating means to which the combustion adjusting means for heating the outer peripheral surface directly under the horizontal rotating cylinder is added. 2. The exhaust gas according to claim 1, wherein each region is divided into three or more regions in the lateral direction, and the temperature of the cylindrical inner wall surface is individually set by adjusting the combustion load for each region. It is a hot air introduction type horizontal rotating cylindrical continuous stirrer, and in the so-called sufficiently long rotating cylinder, due to the nature of heat conduction, the inner wall temperature is in a temperature zone that matches the gas combustion amount of the nearest outer wall to some extent, If the combustion amount is changed for each region, different temperature zones can be set. For example, in the region I shown in FIG. 1 of the examples described later, the average temperature of the inner wall is 230 ° C. with a high fire, 190 ° C. with a low fire in region II, 210 ° C. with a medium fire in region III, or the like. A wide temperature range can be selected in accordance with the temperature range that can reduce scorching.
[0014]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, with reference to FIG. 1 and FIG. 2, apparatus-related equipment conditions related to the exhaust hot air introduction type horizontal rotary cylindrical continuous stirrer of the present invention will be described. FIG. 1 shows a configuration diagram of a horizontal hot-cylindrical continuous stirrer with exhaust hot air introduction according to an embodiment of the present invention, and FIG. 2 shows a side view of a part of the continuous stirrer.
[0015]
As the horizontal cylinder 5, a metal material (for example, steel material, copper-based material, stainless steel, etc.) having a sufficient thickness and sufficient heat conductivity to prevent local burning and average heating without unevenness ), And the inner surface of the cylinder is preferably mirror-finished as much as possible in consideration of cleanability and prevention of scorching, or a Teflon coating or a Teflon impregnation treatment to enable continuous operation for a longer time. Surface treatment such as thermal spraying of metal powder is an effective method.
[0016]
On the inner wall of the cylinder, two or more scraping blades 6 having a height of about 3 to 15 cm for scraping the processing material are attached in the lateral direction and at least one in the circumferential direction. If necessary, the scraping blade 6 may be provided with an angle for sending the material to the discharge side, and there is also a fixing method capable of changing the blade angle. In the case of fry tends material becomes bunching during rotation, mixing, transfer, such as rice products, according to the position to fall as shown in FIG. 2 embodiment, Ru attached detangling grille 7.
[0017]
The cylinder is installed so as to have a slightly downward slope (1/20 to 50) toward the discharge side (however, this is not the case when the material feed angle is provided on the scraping blade 6), and a variable speed drive device 9 is rotated. The residence time of the processing material in the cylinder, the so-called frying time, can be changed by the inclination angle and the rotational speed of the cylinder.
[0018]
In consideration of the efficiency of continuous operation, the ratio of the lateral length of the cylinder to the inner diameter is preferably 3 or more.
[0019]
Three or more gas burners that can adjust combustion in the lateral direction and 1 to 3 in the circumferential direction are arranged on the outer periphery of the rotating cylinder, mainly around the bottom, and the so-called plural burners are used to make small increments. Allows heat load adjustment.
[0020]
Further, it is preferable that the gas supply pipe is divided into regions in the horizontal direction of the cylinder as shown in FIG. 1 of the embodiment, and a gas combustion adjusting valve or an alternative means is provided for each division.
[0021]
A plurality of radiation thermometers 11 or temperature measuring means instead thereof are arranged on the outer wall of the rotating cylinder to perform temperature management and monitoring of the outer wall temperature.
[0022]
As shown in FIG. 2 of the embodiment, a hot air cover 16 that also serves as a heat insulating material is disposed around the rotating cylinder, and the combustion gas rises in the flow path between the outer wall of the cylinder and the cover, and is connected to the duct 17 near the top. Is done. The duct 17 is then branched off from the hot air bypass line 19, and then enters the dust removal filter 21. Next, the duct 17 is combined with fresh air and supplied to the cylinder from the processed product discharge end side of the cylinder. Line A is provided. In addition, the position of a branch, the position of a filter, and the position of fresh air introduction do not stick so much to the order.
[0023]
The hot air bypass line 19 and the fresh air introduction port are respectively provided with dampers 20 and 22 for adjusting the flow rate, or alternative means, and the temperature and air volume of the hot air introduced into the cylinder are set by adjusting the dampers.
[0024]
Unlike the system where the amount of water evaporation is different due to the increase in the material temperature of the material like the batch type, it has never been possible to introduce hot air in the continuous type, so the moisture can be controlled stably. Unevenness can be reduced.
[0025]
The exhaust air coming out from the material input end side is combined with the hot air bypass line 19, then enters the exhaust gas purifier 25, and is released to the atmosphere through the exhaust air fan 26.
[0026]
Three to five thermometers 18 are arranged in a series of hot air lines to manage and monitor the temperature of the hot air.
[0027]
The material to be processed is supplied into the rotating cylinder through the input means such as the raw material input chute 4 or a screw feeder instead thereof.
[0028]
The material is picked up by the scraping blades 6 and falls, disperses, contacts the inner wall, mixes, repeats this, and advances to the discharge side while contacting with hot air and forced convection.
[0029]
The processed product is discharged through the processed product discharge chute 8 or an alternative means.
[0030]
When edible oil is used for stir-cooking, it is supplied into the cylinder by the oil injection pump 3 or a means in place thereof.
[0031]
A front door 23 is provided on the cylinder discharge end side of the cylinder, and is opened during cleaning and inspection in the cylinder.
[0032]
Horizontal rotary cylinder 5, drive unit 9, combustion gas burner 12, heat insulating cover 16, hot air bypass damper 20, fresh air damper 22, hot air bypass line 19, raw material input chute 4, processed product discharge chute 8, front door 23, the exhaust hood 24, the thermometers 11, 18 and the like are preferably installed on the same base as much as possible, and when changing the inclination angle of the rotating cylinder, it is only necessary to change the inclination angle of the base, The above-mentioned auxiliary equipment mounted on the gantry can be left as it is.
[0033]
It is more preferable to provide means that can easily change the inclination angle of the gantry, for example, a jack 28 or a screw with a handle.
[0034]
In addition, for burning off the inner wall of the cylinder after continuous operation for a long time, high-pressure water using a plunger pump with a pressure of about 10 to 20 megapascals as a source is connected to a jet gun, and the jet is rotated while the cylinder is rotated. If the gun is attached to the continuous feeding device and sprayed onto the wall surface, it can be cleaned cleanly with almost no human intervention.
[0035]
【Example】
The present invention will be specifically described with reference to the drawings shown in the embodiments, but some of the equipment conditions and the like described in the previous section are omitted. Note that the present invention is not limited to this.
[0036]
The various materials to be processed are mixed with the edible oil to be used in the raw material fixed supply machine 1 and quantitatively charged into the raw material charging chute 4. On the other hand, edible oil is supplied directly from the oil supply tank 2 to the input chute 4 by the oil supply pump 3 from the metering feeder 1 or the edible oil supply line. The material and cooking oil then enter the raw material input end side of the horizontal rotary cylinder 5.
[0037]
The material that has entered the rotating cylinder 5 that has been heated to a predetermined temperature in advance is scraped up by the scraping blade 6, and proceeds to the processed product discharge end side while repeating dropping, dispersion, contact with the inner wall of the can and mixing uniformly. The residence time of the material is determined by the inclination angle of the cylinder and the rotation speed of the cylinder.
[0038]
When processing an object that tends to be dumpling during the process, such as rice, the loosening grid 7 is attached to the position where the material falls.
[0039]
The material in progress in the rotating cylinder is always in direct contact with hot air introduced from the processed product discharge end side, and so-called counter-current forced convection heat transfer is performed. This forced convection heat transfer efficiently promotes the temperature rise of the material and the evaporation of moisture.
[0040]
The material in progress in the cylinder is fried almost without being dipped in the drip due to the hot air effect, so that a so-called high-quality fried product can be made.
[0041]
The processed product discharged from the discharge end side passes through the processed product discharge chute 8 and is conveyed to a predetermined place by a processed product transfer conveyor or the like.
[0042]
The rotating cylinder 5 uses a variable speed driving device, and conduction to the cylinder is performed by a driving gear 9, and a receiving rotating roller 10 is installed on one side.
The rotating cylinder 5 has a slight downward gradient toward the discharge side of the processed product.
[0043]
Three or more gas burners 12 are arranged in the lateral direction around the outer periphery of the rotating cylinder, mainly around the bottom, and the rotating cylinder 5 is heated by the gas burner.
[0044]
The fuel supply pipes of the gas burners 12 arranged in a plurality in the horizontal direction are divided into three regions in the horizontal direction, and a combustion adjustment valve 13 is provided for each of the zones. This adjusting valve 13 can change the temperature zone of the cylindrical inner wall for each region. This allows operation in the lateral temperature range most suitable for the material.
[0045]
A combustion air supply port 14 and a combustion state inspection port 15 are disposed around the gas burner 12.
[0046]
The combustion gas of the gas burner 12 passes through a flow path between the heat insulating cover 16 and the outer wall of the cylinder 5 and rises to the top while applying heat to the cylinder, and is connected to the duct 17.
[0047]
Next, the hot air branches off from the hot air bypass line 19 and enters the dust removal filter, soot is removed.
The hot air bypass line 19 is provided with a damper 20 for adjusting the flow rate.
[0048]
The hot air coming out of the dust removal filter 21 is then mixed with fresh air and introduced into the processed product discharge end side of the rotating cylinder. The air volume of fresh air is adjusted by the damper 22.
[0049]
The temperature and air volume of the hot air introduced into the rotating cylinder can be set in a wide range by the escape amount to the hot air bypass line (depending on the opening degree of the damper 20) and the fresh air introduction amount (depending on the opening degree of the damper 22).
[0050]
The hot air introduced into the cylinder proceeds to the material input end side while performing forced convection heat transfer with the material, gathers in the exhaust air hood 24, and then joins the hot air bypass line 19, and then cleans the exhaust gas. Proceed to 噐 25.
[0051]
In the wet exhaust gas cleaning tank 25, oily smoke is removed, moisture is added, sucked into the exhaust fan 26, and released into the atmosphere.
[0052]
For measuring the temperature of the outer wall of the cylinder, several radiation thermometers 11 and several hot air thermometers 18 are attached for temperature management and monitoring.
[0053]
This equipment matches the properties of the material such as the degree of thermal denaturation, moisture content, and ease of scorching, and the rotational speed, convection time, combustion load, temperature of the cylinder inner wall, and the temperature range in the horizontal direction of the cylinder inner wall according to the treatment flow rate. The temperature and volume of hot air can be freely changed, and a wide range of operation is possible.
[0054]
A front door 23 is provided on the processed product discharge side for use in cleaning the cylinder or for inspection.
[0055]
On the other hand, the main gantry 27 is equipped with a horizontal rotating cylinder 5 and a driving device for the related device, a gas combustion device, a hot air device, and the like, and the inclination angle of the cylinder is adjusted by an angle adjusting jack 28.
[0056]
【The invention's effect】
The present invention, using a horizontal rotating cylinder type continuous fry machine, introduced into the cylinder to exhaust hot air in the gas combustion by forced convection contact treated product countercurrent, heating and evaporation greatly promoted material As a result, the processing capacity has been greatly improved, high-quality stir-fry that is hardly submerged in the drip, long-time continuous operation by reducing the burning, energy saving, and space saving. Even if a material that tends to be dumpling like rice is fried by attaching a scraping blade to the inner wall of the cylinder and attaching a grid for loosening according to the position where the scraped material falls・ It became possible to fry without mixing into dumplings during mixing and transfer. In addition, this apparatus has a mechanism that can change the temperature of the hot air, the air volume, the temperature of the inner wall of the cylinder, etc. to a high range, and can be operated in a wide range according to the properties of the processing material and the processing flow rate.
[Brief description of the drawings]
FIG. 1 is a diagram showing a configuration of a continuous fried device according to an embodiment of the present invention.
FIG. 2 is a side view of a part of the continuous stirrer.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 ... Raw material fixed supply machine 2 ... Oil supply tank 3 ... Oil supply pump 4 ... Raw material injection chute 5 ... Horizontal rotary cylinder 6 ... Scooping blade 7 ... Unraveling lattice 8 ... Processed product discharge chute 9 ... Cylindrical drive gear 10 ... Rotating roller DESCRIPTION OF SYMBOLS 11 ... Radiation thermometer 12 for outer walls ... Gas burner 13 ... Combustion control valve 14 ... Combustion supply port 15 ... Combustion state inspection port 16 ... Heat insulation cover 17 ... Duct 18 ... Thermometer 19 for hot air ... Hot air bypass line 20 ... Bypass Damper 21 ... Smoke removal filter 22 ... Fresh air damper 23 ... Front door 24 ... Exhaust hood 25 ... Exhaust gas purifier 26 ... Exhaust fan 27 ... Main mount 28 ... Inclination angle adjusting jack 29 ... Processed product conveyor

Claims (3)

横型回転円筒型の連続炒め装置において、円筒外周面の加熱に用いた燃焼ガスの排熱風を回転円筒の内部に導く排熱風供給ラインを配設すると共に、回転円筒内部に導く排熱風を炒め材料の移送方向と逆向きとし、炒め材料と排熱風を向流接触せしめるように、排熱風供給ラインを炒め処理食品排出端側に連接し、該円筒内壁には掻き上げ羽根を取りつけ、掻き上げられた材料が落下する位置に合わせて、ほぐし用格子を取りつけたことを特徴とする排熱風導入型の横型回転円筒式連続炒め装置。In the horizontal rotary cylindrical continuous stirrer, a waste hot air supply line that guides the exhaust heat of the combustion gas used to heat the outer peripheral surface of the cylinder to the inside of the rotary cylinder is provided , and the waste hot air that leads to the inside of the rotary cylinder is stir-fried The waste hot air supply line is connected to the fried food discharge end side so that the stir-fried material and the waste hot air are in countercurrent contact with the transfer direction of the fried food. A horizontal rotating cylindrical continuous stirrer with a hot air introduction type, wherein a lattice for loosening is attached to the position where the material falls. 排熱風供給ラインは、排熱風バイパスラインへの逃がし量及びフレッシュ空気導入量をそれぞれ調整するダンパーに接続しており、それぞれの開度に応じて円筒内部に導入する熱風の温度と風量を設定することを特徴とする請求項1記載の排熱風導入型の横型円筒回転式連続炒め装置。  The exhaust hot air supply line is connected to a damper that adjusts the amount of escape to the exhaust hot air bypass line and the amount of fresh air introduced, and the temperature and air volume of the hot air introduced into the cylinder are set according to the degree of opening. A horizontal cylindrical rotary continuous frying device of the exhaust hot air introduction type according to claim 1. 横型回転円筒の横方向有効長と円筒内径の比が3以上であって、横型回転円筒の直下において外周面を加熱させる燃焼調整手段を付加した加熱手段を円筒の横方向に3区分以上にした領域ごとに個別に設けてあり、それぞれの領域ごとに燃焼負荷を調整して円筒内壁面の温度帯を個別に設定することを特徴とする請求項1記載の排熱風導入型の横型回転円筒式連続炒め装置。  The ratio of the horizontal effective length of the horizontal rotating cylinder to the inner diameter of the cylinder is 3 or more, and the heating means to which the combustion adjusting means for heating the outer peripheral surface directly under the horizontal rotating cylinder is divided into three or more sections in the horizontal direction of the cylinder. The exhaust-air-introduced horizontal rotary cylindrical type according to claim 1, wherein each region is provided individually, and the temperature load of the inner wall surface of the cylinder is individually set by adjusting the combustion load for each region. Continuous stirrer.
JP2000307369A 2000-10-06 2000-10-06 Horizontal rotary cylindrical continuous stirrer with exhaust hot air introduction type Expired - Fee Related JP4117521B2 (en)

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JP2000307369A JP4117521B2 (en) 2000-10-06 2000-10-06 Horizontal rotary cylindrical continuous stirrer with exhaust hot air introduction type
CNB011361158A CN1188042C (en) 2000-10-06 2001-10-08 Lead-in hot air horizohntal rotary cylinder continuous frying apparatus

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JP2000307369A JP4117521B2 (en) 2000-10-06 2000-10-06 Horizontal rotary cylindrical continuous stirrer with exhaust hot air introduction type

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JP4117521B2 true JP4117521B2 (en) 2008-07-16

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