JP2002247963A - Heat treatment apparatus for granular substance - Google Patents

Heat treatment apparatus for granular substance

Info

Publication number
JP2002247963A
JP2002247963A JP2001047492A JP2001047492A JP2002247963A JP 2002247963 A JP2002247963 A JP 2002247963A JP 2001047492 A JP2001047492 A JP 2001047492A JP 2001047492 A JP2001047492 A JP 2001047492A JP 2002247963 A JP2002247963 A JP 2002247963A
Authority
JP
Japan
Prior art keywords
steaming
heat treatment
raw material
granular material
granular
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Withdrawn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
JP2001047492A
Other languages
Japanese (ja)
Inventor
Isoroku Otsuka
五十六 大塚
Misao Kamoshita
操 鴨下
Iwao Niihori
巌 新堀
Nobuyuki Yamamoto
信行 山本
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.)
Yamazaki Mazak Corp
Yamazaki Tekkosho KK
Original Assignee
Yamazaki Tekkosho KK
Yamazaki Machinery Works Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Yamazaki Tekkosho KK, Yamazaki Machinery Works Ltd filed Critical Yamazaki Tekkosho KK
Priority to JP2001047492A priority Critical patent/JP2002247963A/en
Publication of JP2002247963A publication Critical patent/JP2002247963A/en
Withdrawn legal-status Critical Current

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  • Commercial Cooking Devices (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a heat treatment apparatus for granular substances, enabling heat treatment to be efficiently performed by making water content forcedly and uniformly penetrate the inside of granular substances at the stage previous to being charged into a steaming can apparatus so as to inhibit metamorphic unevenness from causing in the steaming can apparatus. SOLUTION: This heat treatment apparatus for granular substances has the following structure: a sprinkler system 19 for watering granular substances supplied via a hopper 10 is attached at the forward of the inlet part 6 of a steaming can apparatus 2, a forcedly penetrating transfer apparatus 3 for making water forcedly penetrate the granular substances by letting them pass through a screw feeder 18 so structured as to make inner pressure increase gradually from its upstream side to its downstream side is attached, and a raw material transferring pressure regulation apparatus 4 provided with a hemispherical valve element 25 having a V-shaped edge 24 between the entering parts 6 respectively of the forcedly penetrating transfer apparatus 3 and the steaming can apparatus 2.

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】本発明は主に醸造原料等とし
て用いられる粉粒物質の加熱処理装置に係り、特に蒸煮
缶装置に連続投入される前段階において粉粒物質の内部
に均一に水分を浸透させるようにすると共に、安定して
粉粒物質を蒸煮缶装置内に供給できるようにして加熱処
理を効率良く行えるようにした粉粒物質の加熱処理装置
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat treatment apparatus for a granular material mainly used as a raw material for brewing and the like, and more particularly to a method for uniformly dispersing moisture inside the granular material at a stage prior to continuous feeding into a steaming can device. The present invention relates to a heat treatment apparatus for a granular material, which is capable of infiltrating and stably supplying the granular material into a steaming can device so that the heat treatment can be efficiently performed.

【0002】[0002]

【従来の技術】本出願人のうち大塚五十六は、特開平9
−275931号公報に示されているように、醸造原料
等として用いられる粉粒物質に関し加水並びに高圧部へ
の投入を連続して行えるようにした粉粒物質の加熱処理
装置を他の発明者らと共同して完成させた。この従来の
加熱処理装置は、同公報に示されているように、原料入
口及び原料排出口を有する加熱機(蒸煮缶装置)、該原
料入口に設けられ軸方向に離間した原料受渡し位置で開
モードとなる空所を画成して原料を搬送する回転機構か
らなり、原料投入装置の原料受入室の下流部に噴射機を
設けた原料投入装置、原料排出口に設けられた原料排出
装置、水分吸収管および絞り部材から構成され、原料投
入装置と加熱機の間に水分吸収管および絞り部材を、前
者を上流側にして順次介装するようにして原料への加水
並びに高圧部への投入を同時に行えるようにしたもので
ある。
2. Description of the Related Art Of the present applicant, Isoroku Otsuka is disclosed in
As disclosed in Japanese Patent No. 275931, a heat treatment apparatus for a granular material used as a brewing material or the like, which can continuously add water and feed into a high-pressure section, was developed by other inventors. Completed in collaboration with. As shown in this publication, this conventional heat treatment apparatus has a heater (steaming can device) having a material inlet and a material outlet, and is opened at a material transfer position provided at the material inlet and spaced apart in the axial direction. A raw material input device provided with an injector downstream of a raw material receiving chamber of the raw material input device, a raw material discharge device provided at a raw material discharge port, comprising a rotation mechanism that defines a space to be a mode and transports raw material; It is composed of a water absorption tube and a throttle member, and the water absorption tube and the throttle member are interposed between the raw material charging device and the heater so that the former is located upstream, and the water is added to the raw material and the high pressure part is charged. Can be performed simultaneously.

【0003】[0003]

【発明が解決しようとする課題】前記従来の粉粒物質加
熱処理装置は、蒸煮缶装置への原料供給が単一種の粉粒
体であっても該粉粒体に対する撒水比率が所定の割合を
下回る場合、または所定の配合割合であっても、粉粒物
質の種類や形態等が異なる場合には原料投入装置の粉粒
物質・水の吸い込み不良および粉粒物質・水の吸い込み
に脈動吸い込みが発生し水分浸透が不均一な撒水粉粒物
質となり次段の蒸煮缶装置での加熱処理に斑が生じるこ
とが判明した。
In the above-mentioned conventional heat treatment apparatus for a granular material, even if the raw material supply to the steaming can device is a single type of granular material, the water spraying ratio for the granular material is a predetermined ratio. If the amount is less than the specified value, or if the type and form of the granular material are different, even if the mixing ratio is the prescribed ratio, poor suction of the granular material and water from the raw material input device and pulsation suction may occur in the suction of the granular material and water. It was found that the sprinkled powder was generated and the water penetration became uneven, resulting in unevenness in the heat treatment in the next-stage steaming can device.

【0004】また、従来装置においては原料に対する加
水は通常のパイプから構成される水分吸収管内を通過中
に行われるため、当該水分吸収管を比較的長尺に設定し
なければならず、一連の作業終了時に当該水分吸収管内
や絞り部材内に湿潤した粉粒物質が多量に残存し、廃棄
処分される原料が増えるという問題点があると共に、変
敗回避のため多量の洗浄水が必要になるという不具合点
がある。
In addition, in the conventional apparatus, the water is added to the raw material while passing through a water absorption tube composed of an ordinary pipe. Therefore, the water absorption tube must be set relatively long, and a series of water absorption is required. At the end of the operation, a large amount of wet particulate matter remains in the water absorption tube and the squeezing member, which increases the amount of raw materials to be disposed of, and requires a large amount of washing water to avoid deterioration. There is a problem.

【0005】さらに、従来装置における絞り部材は蒸煮
缶装置内の加圧蒸気が上流側である水分吸収管に至るの
を防止する一種のシールの役目をするものであって原料
供給が比較的少量の場合には相応の効果を発揮するとし
ても、括れ部の口径は固定されていて変更不可となって
いるため処理量が多大になったり、あるいは所定量より
過少になったりすると蒸煮缶装置に対する連続投入が困
難になるという問題点があった。
[0005] Further, the throttle member in the conventional apparatus serves as a kind of seal for preventing pressurized steam in the steaming can apparatus from reaching the moisture absorption pipe on the upstream side. In the case of, even if it exerts a corresponding effect, the diameter of the constricted portion is fixed and can not be changed, so that the processing amount becomes large, or if it becomes less than the predetermined amount, the steaming can device There has been a problem that continuous feeding becomes difficult.

【0006】本発明者らは、前記した従来装置に伴う不
具合点を解消すべく鋭意研究を重ねた結果、蒸煮缶装置
の入口部の手前に、粉粒物質に水分を強制的に浸透させ
る強制浸透移送装置を付設するようにすれば、従来装置
のようなモーノポンプからなる原料投入装置が不要にな
ると共に、蒸煮缶装置に向けての移送中に粉粒物質の内
部にまで均等に水分を浸透させることができて蒸煮斑の
発生を抑止することができることを知見した。また、蒸
煮缶装置の入口部の手前に水分の強制浸透を可能にする
強制浸透移送装置を設ければ従来のような長尺の水分吸
収管が不要となり作業終了時に無駄となる原料をきわめ
て少なくすることができ、しかも洗浄水も大幅に削減す
ることができることを見出した。さらに、当該強制浸透
移送装置と蒸煮缶装置の入口部の間に、原料送通路の開
度を全開から全閉まで自在に調整することができる原料
送入圧調整装置を設けることにより処理量の多寡並びに
撒水量の変動等に対応して蒸煮缶装置に原料を連続投入
できることを知見し本発明を完成させた。
The inventors of the present invention have conducted intensive studies to solve the problems associated with the above-mentioned conventional apparatus. As a result, a forced forcing of water into the granular material was forced before the inlet of the steaming can apparatus. If a permeation transfer device is added, a raw material input device consisting of a mono pump as in the conventional device is not required, and moisture is evenly penetrated into the inside of the granular material during transfer to the steaming can device. It was found that it was possible to suppress the occurrence of steam spots. In addition, if a forced osmosis transfer device that enables forced osmosis of water is provided in front of the inlet of the steaming can device, a long water absorption tube as in the conventional case becomes unnecessary, and the amount of waste material at the end of the work is extremely reduced. It was found that cleaning water can be greatly reduced. Further, by providing a raw material feed pressure adjusting device capable of freely adjusting the degree of opening of the raw material feed passage from fully open to fully closed between the forced osmosis transfer device and the inlet of the steaming can device, the throughput can be reduced. The present inventors have found that the raw materials can be continuously supplied to the steaming can device in response to the variation in the amount of water and the amount of water sprayed, and completed the present invention.

【0007】従って、本発明は前記した従来装置の不具
合点を解消し、蒸煮缶装置に投入される前段階において
粉粒物質の内部にまで均一に水分を強制浸透させるよう
にして、例えば丸大豆、脱脂大豆等の醸造用原料を飽和
水蒸気ないし過熱水蒸気等の水蒸気で加熱処理し蒸煮缶
装置での蒸煮斑の発生を抑止し加熱処理を効率良く行え
るようにすると共に、蒸煮缶装置内の加圧蒸気が上流側
に逆流するのを有効に防止して、原料の連続投入を可能
にした粉粒物質の加熱処理装置を提供することを目的と
するものである。
Therefore, the present invention solves the above-mentioned disadvantages of the conventional apparatus, and forcibly penetrates moisture even into the inside of the granular material before it is put into the steaming can apparatus. In addition, brewing raw materials such as defatted soybeans are heat-treated with steam such as saturated steam or superheated steam to suppress the occurrence of steam spots in the steaming can device so that the heating process can be performed efficiently and the heating process in the steaming can device is performed. It is an object of the present invention to provide a heat treatment apparatus for a granular material, which can effectively prevent a backflow of pressurized steam to an upstream side and enable continuous input of raw materials.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するため
の本発明の構成を詳述すれば、請求項1に係る発明は、
入口部を介して投入される醸造原料の如き粉粒物質の出
口部に向けての缶内移送中に、当該缶内に供給される飽
和水蒸気ないし過熱水蒸気によって当該粉粒物質を加熱
処理するようにした蒸煮缶装置を含む加熱処理装置にお
いて、当該蒸煮缶装置の入口部の手前に、ホッパーを通
じて供給される粉粒物質に撒水を施すための撒水装置を
付設すると共に、上流側から下流側に向け徐々に内圧が
上昇するようになっているスクリューフィーダー内を通
すことによって粉粒物質に水分を強制的に浸透させる強
制浸透移送装置を付設して蒸煮缶装置での加熱処理を効
率良く行えるようにしたことを特徴とする粉粒物質の加
熱処理装置である。
The structure of the present invention for achieving the above object is described in detail below.
During the transfer of the granular material, such as a brewing material supplied through the inlet portion, to the outlet portion in the can, the granular material is heated by saturated steam or superheated steam supplied into the can. In the heat treatment apparatus including the steaming can device, a water spraying device for spraying the granular material supplied through the hopper is provided in front of the inlet portion of the steaming can device, and from the upstream side to the downstream side. A forced infiltration transfer device that forcibly permeates moisture into the granular material by passing through a screw feeder whose internal pressure gradually rises toward A heat treatment apparatus for a granular material, characterized in that:

【0009】また、請求項2に係る発明は、前記強制浸
透移送装置と蒸煮缶装置の入口部の間に、V字形のエッ
ジを有する半球状の弁体を弁ケース内で回転させること
により原料送通路の開度を全開から全閉まで自在に調整
することができる原料送入圧調整装置を介装したことを
特徴とする請求項1記載の粉粒物質の加熱処理装置であ
る。
Further, the invention according to claim 2 is characterized in that a hemispherical valve body having a V-shaped edge is rotated in the valve case between the forced osmosis transfer device and the inlet of the steaming can device. 2. The heat treatment apparatus for a granular material according to claim 1, further comprising a raw material feed pressure adjusting device capable of freely adjusting an opening degree of the feed passage from full opening to full closing.

【0010】ホッパーを通じて原料受入部に供給される
粉粒物質は、上流側から下流側に向け徐々に内圧が上昇
するようになっているスクリューフィーダー、すなわ
ち、スクリューピッチが上流側から下流側に向け徐々に
狭くなっていると共に、軸心の径が上流側から下流側に
向け徐々に太くなっていてフイーダー管と軸心及びスク
リュー羽根によって画成される原料移送室が徐々に狭隘
となっている特殊構造のスクリューフィーダー内を通る
際に撒水装置によって供給された水分が強制的に粉粒物
質の内部にまで均一に浸透し、蒸煮缶装置での加熱処理
が効率良く行えるようになる。
The particulate matter supplied to the raw material receiving section through the hopper is supplied to a screw feeder whose internal pressure gradually increases from the upstream side to the downstream side, that is, the screw pitch is changed from the upstream side to the downstream side. As the diameter gradually decreases, the diameter of the shaft gradually increases from the upstream side to the downstream side, and the material transfer chamber defined by the feeder tube, the shaft center, and the screw blades gradually narrows. The water supplied by the water sprinkling device when passing through the screw feeder having a special structure is forcibly and uniformly penetrated into the inside of the granular material, so that the heat treatment in the steaming can device can be efficiently performed.

【0011】また、スクリューフィーダーからなる強制
浸透移送装置と蒸煮缶装置の入口部の間に、原料送通路
の開度を全開から全閉まで自在に調整することができる
弁体を具備した原料送入圧調整装置を設けることによっ
て、粉粒物質の種類や形態、あるいは処理量に応じて開
度を自在に調整することができ、蒸煮缶装置内の加圧蒸
気が逆流するのを有効に防止することができ蒸煮缶装置
への原料投入を安定した状態で行うことができるように
なる。
[0011] Further, between the forced osmosis transfer device comprising a screw feeder and the inlet of the steaming can device, the raw material feeder provided with a valve body capable of freely adjusting the opening degree of the raw material feed passage from fully open to fully closed. By providing an input pressure adjusting device, the degree of opening can be freely adjusted according to the type and form of the granular material, or the processing amount, and the backflow of pressurized steam in the steaming can device is effectively prevented. Therefore, it is possible to stably feed the raw materials to the steaming can device.

【0012】[0012]

【発明の実施の形態】以下、本発明に係る粉粒物質の加
熱処理装置の具体的構成を図示の実施例に基づき詳細に
説明する。図1は本発明加熱処理装置の全体を示す概略
図、図2は蒸煮缶装置の手前に付設されるスクリューフ
ィーダーからなる強制浸透移送装置の詳細を示す説明
図、図3は原料送入圧調整装置の説明図である。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, a specific configuration of a heat treatment apparatus for a granular material according to the present invention will be described in detail based on the illustrated embodiment. FIG. 1 is a schematic diagram showing the entire heat treatment apparatus of the present invention, FIG. 2 is an explanatory view showing details of a forced osmosis transfer device comprising a screw feeder attached to the front of a steaming can device, and FIG. It is explanatory drawing of an apparatus.

【0013】図中1は醸造原料である丸大豆、脱脂大豆
等の粉粒物質の加熱処理装置の全体を示し、飽和水蒸気
あるいは過熱水蒸気等の水蒸気によってこれらを加熱処
理し次工程へ送る装置であり、主に蒸煮缶装置2と、当
該蒸煮缶装置2の前段階に付設され、蒸煮缶装置2によ
る変性等加熱処理の容易化と完全性並びに定量供給を担
保するための強制浸透移送装置3及び原料送入圧調整装
置4とから構成されており、強制浸透移送装置3と原料
送入圧調整装置4の位置関係は、前者の方が原料の流れ
に沿って上流側に設置される。
In FIG. 1, reference numeral 1 denotes an entire apparatus for heat-treating granular materials such as round soybeans and defatted soybeans, which are brewing raw materials, which is heated by steam such as saturated steam or superheated steam and sent to the next step. Yes, the steaming can device 2 and a forced osmotic transfer device 3 attached to a stage preceding the steaming can device 2 for facilitating heat treatment such as denaturation by the steaming can device 2 and ensuring completeness and quantitative supply. And the raw material feeding pressure adjusting device 4. The positional relationship between the forced osmotic transfer device 3 and the raw material feeding pressure adjusting device 4 is such that the former is installed upstream along the flow of the raw material.

【0014】先ず、蒸煮缶装置2は円筒状をなす缶胴5
の一端上部に原料の入口部6を付設すると共に、缶胴5
の他端下部に加熱処理済み原料の出口部7を突成し、缶
胴5の内部には入口部6を通じて投入される原料を出口
部7側に向けて一定速度で移送するスクリューコンベヤ
やネットコンベヤ等からなる移送手段8を配設してあっ
て、蒸気吹込管9を通じて缶胴5内に供給される飽和水
蒸気あるいは過熱水蒸気等によって原料を移送中に、た
とえば0.1〜6Kg/cm2 程度の加圧状態で加熱処
理するものである。
First, the steaming can device 2 has a cylindrical can body 5.
A raw material inlet 6 is attached to the upper end of the
At the lower end of the other end, a heat-treated material outlet 7 is formed, and a screw conveyor or a net is provided inside the can body 5 for transferring the material supplied through the inlet 6 at a constant speed toward the outlet 7 side. A transfer means 8 composed of a conveyor or the like is provided, and the raw material is transferred by saturated steam or superheated steam supplied into the can body 5 through the steam blowing pipe 9, for example, 0.1 to 6 kg / cm 2. The heat treatment is carried out in a pressure state of a certain degree.

【0015】強制浸透移送装置3は、ホッパー10を通
じて供給される粉粒物質原料に、水分を強制的に浸透さ
せながら下流側に原料を送り出すための装置であり、ホ
ッパー10から投入される原料を受け入れるための一次
チャンバー11を画成する略逆T字状の原料受入部フィ
ーダーケーシング12と、この原料受入部フィーダーケ
ーシング12に連設される横長のフィーダー管13と、
このフィーダー管13内において同心的に回転駆動する
よう配設されるスパイラルスクリュー14等から構成さ
れる。
The forced osmosis transfer device 3 is a device for sending out the raw material to the downstream side while forcibly infiltrating moisture into the granular material raw material supplied through the hopper 10. A substantially inverted T-shaped feeder casing 12 defining a primary chamber 11 for receiving the feeder casing 12, a horizontally long feeder tube 13 connected to the feeder casing 12,
The feeder tube 13 includes a spiral screw 14 and the like which are arranged to rotate concentrically.

【0016】スパイラルスクリュー14のピッチは図2
に示すように上流側から下流側に向け徐々に狭くなって
いると共に、軸心15の径は上流側から下流側に向け徐
々に太くなるように形成されており、フィーダー管13
の内周面と軸心15の外周面及びスクリュー羽根16の
表面によって画成される原料移送室17は上流側から下
流側に向け徐々に狭隘なスペースとなっている。さら
に、原料移送室17の終点部にはコーン状のスクリュー
フィーダー出口原料絞り部29が形成されているので、
原料が収容された原料移送室17内の圧力は上流側から
下流側に向け徐々に内圧が上昇するようになる。原料が
このような特殊構造のスクリューフィーダー18内を通
過する際に撒水装置19によって供給された水分は強制
的に粉粒物質の内部にまで均一に浸透し、蒸煮缶装置2
における加熱処理は斑なく容易且つ完全に行われるよう
になる。
The pitch of the spiral screw 14 is shown in FIG.
As shown in FIG. 3, the diameter of the shaft 15 is gradually increased from the upstream side to the downstream side, and the diameter of the shaft 15 is gradually increased from the upstream side to the downstream side.
The material transfer chamber 17 defined by the inner peripheral surface of the shaft, the outer peripheral surface of the shaft 15 and the surface of the screw blade 16 is a gradually narrow space from the upstream side to the downstream side. Further, a cone-shaped screw feeder outlet raw material narrowing section 29 is formed at the end point of the raw material transfer chamber 17, so that
The internal pressure of the raw material transfer chamber 17 containing the raw material gradually increases from the upstream side to the downstream side. When the raw material passes through the screw feeder 18 having such a special structure, the water supplied by the water sprinkling device 19 is forcibly and uniformly penetrated into the inside of the granular material.
Is easily and completely performed without unevenness.

【0017】なお、図示する撒水装置19はホッパー1
0の下端部付近に噴孔を下向きにして取付けた水噴射管
となっているが、取付箇所についてはこれに限定される
ものではなく、要はスクリューフィーダー18内を通す
前段階において粉粒物質原料に均一に撒水できる位置で
あれば、前記一次チャンバー11内に通じる原料受入部
フィーダーケーシング12に撒水装置19を付設するよ
うにしても一向に差し支えない。また、撒水装置19を
なす水噴射管の付設個数についても、粉粒物質に満遍な
く撒水するため複数個を設置するようにしてもよい。
The water sprinkling device 19 shown in FIG.
The water jet pipe is attached near the lower end of the screw feeder with the injection hole facing downward. However, the mounting location is not limited to this. At a position where water can be evenly sprayed on the raw material, a water spraying device 19 may be attached to the raw material receiving portion feeder casing 12 communicating with the primary chamber 11. Further, a plurality of water injection pipes constituting the water spraying device 19 may be provided in order to spray water evenly to the granular material.

【0018】その他、図2において20は軸心15を回
転駆動させるためのモーター、21は軸心15の回転速
度を制御するギヤボックス、22は原料送出口23に至
る二次チャンバーであり、前記一次チャンバー11から
当該二次チャンバー22に至るまでの間を三等分すれ
ば、最初の部分は原料の送り込み部、中間部は原料の中
圧部、最後の部分は原料の高圧部ということができる。
In addition, in FIG. 2, reference numeral 20 denotes a motor for rotating the shaft 15, 21 denotes a gear box for controlling the rotation speed of the shaft 15, and 22 denotes a secondary chamber leading to a material feed port 23. If the interval from the primary chamber 11 to the secondary chamber 22 is divided into three equal parts, the first part is the feed part of the raw material, the middle part is the medium pressure part of the raw material, and the last part is the high pressure part of the raw material. it can.

【0019】強制浸透移送装置3の高圧部から送り出さ
れる粉粒物質は内部にまで水分が均一に浸透し、蒸煮に
最も適した状態となる。次いで、これを蒸煮缶装置2に
向けて送り出すのであるが、蒸煮缶装置2の内部は蒸気
吹込管9を通じて缶胴5内に供給される飽和水蒸気ない
し過熱水蒸気等によって高圧状態であり、蒸煮缶装置2
内の飽和水蒸気ないし過熱水蒸気等の水蒸気が逆流する
と原料の供給形態が成立しなくなる。
The granular material sent out from the high-pressure section of the forced osmosis transfer device 3 is uniformly infiltrated with water to the inside, and is in a state most suitable for steaming. Next, this is sent out to the steaming can device 2. The inside of the steaming can device 2 is in a high pressure state by saturated steam or superheated steam supplied into the can body 5 through the steam blowing pipe 9. Device 2
When the steam such as the saturated steam or the superheated steam flows backward, the supply form of the raw material cannot be established.

【0020】このような問題点を解消するため、本発明
装置においては、強制浸透移送装置3と蒸煮缶装置2の
入口部6の間に、V字形のエッジ24を有する半球状の
弁体25を弁ケース26内で回転制御することにより原
料送通路27の開度を全開から全閉まで自在に制御する
ことができる原料送入圧調整装置4を介装させるように
した。
In order to solve such a problem, in the apparatus of the present invention, a hemispherical valve body 25 having a V-shaped edge 24 is provided between the forced osmosis transfer device 3 and the inlet 6 of the steaming can device 2. Is controlled in the valve case 26 to control the opening degree of the raw material supply passage 27 from full open to full close.

【0021】すなわち、蒸煮缶装置2内に原料を安定し
て投入するためには、蒸煮缶装置2の入口部6より上流
側の圧力が蒸煮缶装置2内の圧力を上回るようにしてや
ればよいわけであり、蒸煮缶装置2内の圧力が高圧の場
合には原料送入圧調整装置4を制御して弁体25を回転
させ原料送通路27の開度を絞るようにする。逆に、蒸
煮缶装置2内の圧力がそれ程高くない場合には弁体25
を制御して開度を拡げるようにする。また、処理量の多
寡、あるいは粉粒物質の種類等に対応して弁体25の開
度調整を行うようにする。なお、原料送入圧調整装置4
はこのようにV字形のエッジ24を有する弁体25を用
いているので弁体閉止の際に繊維質を多量に含む粉粒物
質を完全に切断することができ原料送通路27を完璧に
遮断することも可能である。
That is, in order to stably feed the raw materials into the steaming can device 2, the pressure upstream of the inlet 6 of the steaming can device 2 should be higher than the pressure in the steaming can device 2. That is, when the pressure in the steaming can device 2 is high, the material feed pressure adjusting device 4 is controlled to rotate the valve body 25 to reduce the opening of the material feed passage 27. Conversely, if the pressure in the steaming can device 2 is not so high, the valve body 25
Is controlled to increase the opening. Further, the opening degree of the valve body 25 is adjusted in accordance with the amount of the processing amount or the type of the granular material. It should be noted that the raw material feeding pressure adjusting device 4
Uses the valve body 25 having the V-shaped edge 24 as described above, so that when the valve body is closed, the particulate material containing a large amount of fibrous material can be completely cut, and the raw material feed passage 27 is completely shut off. It is also possible.

【0022】その他、図中の28は強制浸透移送装置3
と原料送入圧調整装置4の間に必要に応じて介装させる
容積型ポンプ等からなる定量供給装置である。本発明装
置では、ホッパー10に投入された原料は強制浸透移送
装置3を通過する際に加圧され一定の圧力上昇が得られ
るので、前記した原料送入圧調整装置4による原料送通
路27の開度調整により安定して蒸煮缶装置2内に原料
を送り出すことができる。そのため、通常の長尺パイプ
からなる水分吸収管を用いる従来装置では不可欠であっ
た定量供給装置の必要性は低下したが、蒸煮缶装置入口
部6への原料安定供給を一層確実なものとするため選択
的に容積型ポンプ等からなる定量供給装置28を強制浸
透移送装置3と原料送入圧調整装置4の間に付設するよ
うにしてもよい。
In addition, reference numeral 28 in the figure denotes a forced osmosis transfer device 3.
A fixed-quantity supply device comprising a positive displacement pump and the like interposed as necessary between the feed pressure adjusting device 4 and the feed pressure adjusting device 4. In the apparatus of the present invention, the raw material charged into the hopper 10 is pressurized when passing through the forced osmosis transfer device 3 and a constant pressure rise is obtained. The raw material can be stably fed into the steaming can device 2 by adjusting the opening degree. For this reason, the necessity of the quantitative supply device which has been indispensable in the conventional device using the water absorption tube formed of a normal long pipe has been reduced, but the stable supply of the raw material to the inlet 6 of the steaming can device is further ensured. For this purpose, a fixed-quantity supply device 28 composed of a positive displacement pump or the like may be selectively provided between the forced osmosis transfer device 3 and the raw material feeding pressure adjusting device 4.

【0023】本発明粉粒物質の加熱処理装置は以上のよ
うな構成からなり、ホッパー10を介して供給される粉
粒物質原料は撒水装置19から噴射される水と混ざりな
がら次段のスクリューフィーダー18の送り込み部、中
圧部及び高圧部を通過中に、水分が原料の内部組織にま
で浸透する。水分を充分に含浸した原料は二次チャンバ
ー22を通じ、図示する実施形態では定量供給装置28
を介して次段の原料送入圧調整装置4に送られる。ここ
で一定の開度に調整された原料送通路27を通じて入口
部6より蒸煮缶装置2内に投入され、移送手段8による
缶内移送中に蒸気吹込管9を通じて缶胴5内に供給され
る飽和水蒸気等によって加熱処理が行われる。なお、本
発明に係る加熱処理装置は醸造用原料の加熱変性処理以
外にも、例えば食品廃棄物の資源化装置、あるいは均一
な加熱処理が要求される諸種の食品加工分野においても
用いることができる。
The heat treatment apparatus for the particulate material of the present invention has the above-mentioned structure. The raw material of the particulate material supplied through the hopper 10 is mixed with the water jetted from the water sprinkler 19 while the screw feeder of the next stage is mixed. While passing through the feeding section, the medium pressure section and the high pressure section of 18, the water permeates into the internal structure of the raw material. The raw material sufficiently impregnated with moisture passes through the secondary chamber 22 and, in the illustrated embodiment, a metering device 28.
Is sent to the raw material feeding pressure adjusting device 4 at the next stage. Here, the raw material is introduced into the steaming can device 2 from the inlet 6 through the raw material feed passage 27 adjusted to a certain opening degree, and is supplied into the can body 5 through the steam blowing pipe 9 during the transfer in the can by the transfer means 8. Heat treatment is performed with saturated steam or the like. In addition, the heat treatment apparatus according to the present invention can be used in, for example, a resource recycling apparatus for food waste, or various kinds of food processing fields requiring uniform heat treatment, in addition to the heat denaturation treatment of the brewing raw material. .

【0024】[0024]

【発明の効果】本発明粉粒物質の加熱処理装置によれ
ば、蒸煮缶装置に連続投入される前段階において強制浸
透移送装置を設けたので、粉粒物質に対する撒水比率が
所定の割合を下回るような場合であっても、該粉粒体の
内部組織にまで均一に水分を浸透させることができ、蒸
煮缶装置による加熱処理が良好に行われ、蒸煮斑の発生
を有効に抑止することができる。また、従来装置のよう
な長尺の水分吸収管が不要となるので作業終了時に無駄
となる原料をきわめて少なくすることができると共に、
洗浄水も大幅に削減することができ環境保全にも効果が
ある。さらに、当該強制浸透移送装置と蒸煮缶装置の入
口部の間に、原料送通路の開度を全開から全閉まで自在
に調整することができる原料送入圧調整装置を設けるこ
とにより処理量等に変動があったとしても安定した状態
で蒸煮缶装置に原料を連続投入することができる。
According to the heat treatment apparatus of the present invention, since the forced osmosis transfer device is provided in the stage before being continuously charged into the steaming can device, the ratio of water sprayed on the granular material is lower than a predetermined ratio. Even in such a case, it is possible to uniformly infiltrate the water into the internal structure of the granular material, the heat treatment by the steaming can device is performed well, and the occurrence of steaming spots can be effectively suppressed. it can. In addition, since a long water absorption tube as in the conventional apparatus is not required, the amount of waste materials at the end of the work can be extremely reduced, and
Wash water can be greatly reduced, which is effective for environmental protection. Further, by providing a raw material feeding pressure adjusting device between the forced osmotic transfer device and the inlet portion of the steaming can device, which can freely adjust the opening degree of the raw material feeding passage from fully open to fully closed, the processing amount, etc. The raw material can be continuously charged into the steaming can device in a stable state even if the temperature varies.

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

【図1】本発明に係る加熱処理装置の全体を示す概略図
である。
FIG. 1 is a schematic view showing an entire heat treatment apparatus according to the present invention.

【図2】蒸煮缶装置の手前に付設されるスクリューフィ
ーダーからなる強制浸透移送装置の詳細を示す説明図で
ある。
FIG. 2 is an explanatory diagram showing details of a forced osmosis transfer device including a screw feeder attached to the front of a steaming can device.

【図3】原料送入圧調整装置の説明図である。FIG. 3 is an explanatory diagram of a raw material feeding pressure adjusting device.

【符号の説明】[Explanation of symbols]

1:加熱処理装置 2:蒸煮缶装置 3:強制浸透移送装置 4:原料送入圧調
整装置 5:缶胴 6:入口部 7:出口部 8:移送手段 9:蒸気吹込管 10:ホッパー 11:一次チャンバー 12:原料受入部
フィーダーケーシング 13:フィーダー管 14:スパイラル
スクリュー 15:軸心 16:スクリュー
羽根 17:原料移送室 18:スクリュー
フィーダー 19:撒水装置 20:モーター 21:ギヤボックス 22:二次チャン
バー 23:原料送出口 24:V字形エッ
ジ 25:弁体 26:弁ケース 27:原料送通路 28:定量供給装
置 29:スクリューフィーダー出口原料絞り部
1: Heat treatment device 2: Steaming can device 3: Forced osmosis transfer device 4: Raw material feeding pressure adjustment device 5: Can body 6: Inlet portion 7: Outlet portion 8: Transfer means 9: Steam blowing pipe 10: Hopper 11: Primary chamber 12: feeder casing 13: feeder tube 14: spiral screw 15: shaft 16: screw blade 17: feeder chamber 18: screw feeder 19: water spray device 20: motor 21: gear box 22: secondary chamber 23: Raw material feed port 24: V-shaped edge 25: Valve body 26: Valve case 27: Raw material feed path 28: Quantitative supply device 29: Screw feeder outlet raw material throttle section

フロントページの続き (72)発明者 新堀 巌 埼玉県川口市西川口6丁目9番18号 株式 会社山崎鉄工所内 (72)発明者 山本 信行 埼玉県川口市西川口6丁目9番18号 株式 会社山崎鉄工所内 Fターム(参考) 4B039 LC03 LC16 LP03 LP10 4B054 AA17 AB03 BA02 CC04 CC05 CC13 CC18 CC19 CD03 CG06Continued on the front page (72) Inventor Iwao Niibori 6-9-18 Nishikawaguchi, Kawaguchi City, Saitama Prefecture Inside Yamazaki Iron Works Co., Ltd. (72) Inventor Nobuyuki Yamamoto 6-9-18 Nishikawaguchi, Kawaguchi City, Saitama Prefecture Co., Ltd. Yamazaki Iron Works Co., Ltd. F-term (reference) 4B039 LC03 LC16 LP03 LP10 4B054 AA17 AB03 BA02 CC04 CC05 CC13 CC18 CC19 CD03 CG06

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 入口部を介して投入される醸造原料の如
き粉粒物質の出口部に向けての缶内移送中に、当該缶内
に供給される飽和水蒸気ないし過熱水蒸気によって当該
粉粒物質を加熱処理するようにした蒸煮缶装置を含む加
熱処理装置において、当該蒸煮缶装置の入口部の手前
に、ホッパーを通じて供給される粉粒物質に撒水を施す
ための撒水装置を付設すると共に、上流側から下流側に
向け徐々に内圧が上昇するようになっているスクリュー
フィーダー内を通すことによって粉粒物質に水分を強制
的に浸透させる強制浸透移送装置を付設して蒸煮缶装置
での加熱処理を効率良く行えるようにしたことを特徴と
する粉粒物質の加熱処理装置。
1. During the transfer of a granular material such as a brewing material fed through an inlet portion into a can toward an outlet portion, the granular or granular material is supplied by saturated steam or superheated steam supplied into the can. In a heat treatment apparatus including a steaming can device adapted to heat-treat a steaming can device, a watering device for watering the granular material supplied through the hopper is provided in front of the inlet portion of the steaming can device, and Heat treatment in a steaming can device with a forced infiltration transfer device that forcibly permeates moisture into the granular material by passing through a screw feeder whose internal pressure gradually rises from the side to the downstream side A heat treatment apparatus for a granular material, wherein the heat treatment can be performed efficiently.
【請求項2】 強制浸透移送装置と蒸煮缶装置の入口部
の間に、V字形のエッジを有する半球状の弁体を弁ケー
ス内で回転させることにより原料送通路の開度を全開か
ら全閉まで自在に調整することができる原料送入圧調整
装置を介装したことを特徴とする請求項1記載の粉粒物
質の加熱処理装置。
2. A raw material feed passage is opened from full open to full by rotating a hemispherical valve body having a V-shaped edge in a valve case between a forced osmotic transfer device and an inlet of a steaming can device. 2. The apparatus for heat-treating a granular material according to claim 1, further comprising a raw material feeding pressure adjusting device capable of freely adjusting the closed state.
JP2001047492A 2001-02-23 2001-02-23 Heat treatment apparatus for granular substance Withdrawn JP2002247963A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001047492A JP2002247963A (en) 2001-02-23 2001-02-23 Heat treatment apparatus for granular substance

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001047492A JP2002247963A (en) 2001-02-23 2001-02-23 Heat treatment apparatus for granular substance

Publications (1)

Publication Number Publication Date
JP2002247963A true JP2002247963A (en) 2002-09-03

Family

ID=18908908

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001047492A Withdrawn JP2002247963A (en) 2001-02-23 2001-02-23 Heat treatment apparatus for granular substance

Country Status (1)

Country Link
JP (1) JP2002247963A (en)

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