JP3149761U - Shellfish processing system - Google Patents

Shellfish processing system Download PDF

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JP3149761U
JP3149761U JP2009000438U JP2009000438U JP3149761U JP 3149761 U JP3149761 U JP 3149761U JP 2009000438 U JP2009000438 U JP 2009000438U JP 2009000438 U JP2009000438 U JP 2009000438U JP 3149761 U JP3149761 U JP 3149761U
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shellfish
furnace
processing system
calcium oxide
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矢野 秀夫
秀夫 矢野
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矢野 秀夫
秀夫 矢野
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Abstract

【課題】処理効率の向上、CO2の排出抑制、運転管理の労力低減、長時間運転に耐えうる耐久性を可能にした貝類処理システムを提供する。【解決手段】貝類を水洗する脱塩洗浄装置1と、海生物を粗砕する粗砕装置3と、粗砕片を加熱乾燥させる加熱乾燥装置4と、平面視円形経路の炉室内の移動床式の基盤上を通過させて半焼成小砕片を焼成する抵抗型電気炉5と、焼成で得られた酸化カルシウムを収集して袋に詰める袋詰め装置7を具備する。【選択図】図1The present invention provides a shellfish processing system capable of improving processing efficiency, suppressing CO2 emission, reducing operation management labor, and durability capable of withstanding long-time operation. A desalting and cleaning apparatus 1 for washing shellfish with water, a crushing apparatus 3 for crushing marine organisms, a heating and drying apparatus 4 for heating and drying coarse fragments, and a moving bed type in a furnace chamber having a circular path in plan view. A resistance-type electric furnace 5 for firing the semi-fired small pieces by passing over the substrate, and a bagging device 7 for collecting and packing the calcium oxide obtained by the firing. [Selection] Figure 1

Description

本考案は、海産の貝類或いは介類(貝や甲殻類等の甲羅を持つ動物)を対象とした回転移動床式の電気炉であって、対象物(貝類又は介類)を産業廃棄物としたときの最終処分炉であると共に、対象物の高温処理(焼成)によって酸化カルシウムを得る焼成炉を含んだ貝類処理システムに関する。   The present invention is a rotary moving floor electric furnace for marine shellfish or shellfish (animals with shells such as shellfish and shellfish), and the object (shellfish or shellfish) is treated as industrial waste. The present invention relates to a shell processing system that includes a firing furnace that obtains calcium oxide by high-temperature treatment (firing) of an object as well as a final disposal furnace.

各地に残る貝塚にみられるように、人々が貝類を食する際には必ずその貝殻が廃棄物として捨てられてきた。この貝殻の処分については過去に多くの人々がその処分方法について悩んで来た経緯がある。このように廃棄物として行き場の無いものに対して近年有効な処分後の副産物の利用方法の研究が進んでいる。   As can be seen in the shell mounds that remain in various places, when people eat shellfish, the shells have always been discarded as waste. Regarding the disposal of this shell, many people have been worried about the disposal method in the past. In recent years, research on how to use by-products after disposal that is effective for waste that has nowhere to go is progressing.

例えば従来、貝殻生石灰を製造する竪型石灰焼成炉として、竪型石灰焼成炉の原料投入管を炉内挿入部分のない構造とし、排鉱機部の回転シール部を二重構造として、吹き込み空気量の調節機構を備えた冷却用配管を設けたものが開示される(例えば特許文献1参照)。   For example, as a conventional vertical calcination furnace for producing shell lime, the raw material input pipe of the vertical lime baking furnace has a structure with no insertion part in the furnace, and the rotary seal part of the ore excavator part has a double structure and blown air What provided the piping for cooling provided with the adjustment mechanism of quantity is disclosed (for example, refer patent document 1).

特許第3076432号公報Japanese Patent No. 3076432

しかしながら、上記竪型石灰焼成炉は貝殻の処理能力が25トン/日程度の小型の独楽型石灰焼成炉であり、固定床式であって連続処理することはできない。また炉内に配置した焼成帯を高温に保持して焼成するものであるため、7時間もの炉内滞留時間が必要となり、効率的に処理できるものではない。またこの種の焼成帯は通常、オイルやガスによる燃焼熱を熱源とするため、COの排出を伴い、処理量を増やした場合には将来的なCOの削減目標などの社会的要求にこたえることが困難となる。 However, the vertical lime firing furnace is a small self-contained lime firing furnace having a shell processing capacity of about 25 tons / day, and is a fixed bed type and cannot be continuously treated. Further, since the firing zone disposed in the furnace is fired while being kept at a high temperature, a residence time in the furnace of 7 hours is required, and it cannot be efficiently processed. In addition, since this type of firing zone usually uses combustion heat from oil or gas as a heat source, it is accompanied by CO 2 emissions, and if the processing amount is increased, it will meet social demands such as future CO 2 reduction targets. It becomes difficult to answer.

すなわち日々多くの貝類を処理する為には処理能力から連続炉を構成する必要があるが、この連続炉を構成する場合には、処理効率の向上という課題のほか、COの排出抑制という課題や、処理状態ないしメンテナンスといった運転管理の労力低減という課題、また長時間運転に耐えうるだけの耐久性といった課題が生じる。 In other words, in order to process many shellfish every day, it is necessary to configure a continuous furnace from the processing capacity, but in the case of configuring this continuous furnace, in addition to the problem of improving the processing efficiency, the problem of suppressing CO 2 emissions. In addition, there are problems such as reduction of operation management labor such as processing state and maintenance, and durability that can withstand long-time operation.

本考案は上記課題を解決すべく考案された貝類の処理システムであって、以下(1)〜(8)の手段を採用している。   The present invention is a shellfish processing system devised to solve the above problems, and adopts the following means (1) to (8).

(1)本考案の貝類処理システムは、海産の貝類を連続的に処理して酸化カルシウムO5を生産する貝類処理システムであって、
貝類を水洗することで付着塩類を除去して脱塩貝類を得る脱塩洗浄装置1と、
脱塩貝類を粗砕して粗砕片を得る粗砕装置3と、
本処理前の前処理として粗砕片を加熱乾燥させて半焼成片を得る加熱乾燥装置4と、
本処理として所定の平面経路状に伸びる炉室内に備えた移動床式の基盤52上で半焼成片を焼成し、酸化カルシウムO5を得ると共にそれ以外の構成材を焼却する抵抗型電気炉5と、
酸化カルシウムO5を収集して収容袋内に密封する袋詰め装置7を具備してなることを特徴とする。
(1) The shellfish processing system of the present invention is a shellfish processing system that continuously processes marine shellfish to produce calcium oxide O5.
A demineralization washing apparatus 1 for removing demineralized shellfish by removing the attached salt by washing the shellfish with water;
A crushing apparatus 3 for crushing demineralized shellfish to obtain coarse fragments,
A heating and drying device 4 that heat-drys the coarsely crushed pieces as a pretreatment before this treatment to obtain a semi-fired piece;
A resistance-type electric furnace 5 for firing a semi-fired piece on a moving bed type base 52 provided in a furnace chamber extending in a predetermined planar path as a main treatment to obtain calcium oxide O5 and incinerate other constituent materials; ,
It is characterized by comprising a bagging device 7 that collects calcium oxide O5 and seals it in a storage bag.

上記構成のうち、少なくとも脱塩洗浄装置1と粗砕装置3と抵抗型電気炉5という構成の組み合わせによって、脱塩による余分な塩類の付着の除去、粗砕による貝類の大きさや形状の均一化を行って、本炉である抵抗型電気炉5で加熱処理することで、加熱時の「はじけ現象」を防止し、連続的な長時間の処理を行うことができる。この構成においてさらに加熱乾燥装置4を設けることで、連続運転において確実に貝類を処理することができる。またさらに袋詰め装置7を設けることで、得られた酸化カルシウムO5を良好な状態で保管することができる。   Of the above-described configurations, at least a combination of the configuration of the desalting cleaning device 1, the coarse crushing device 3, and the resistance electric furnace 5 removes the adhesion of excess salts by desalting and makes the size and shape of shellfish uniform by rough crushing. By performing the heat treatment in the resistance type electric furnace 5 which is the main furnace, the “flicking phenomenon” at the time of heating can be prevented, and continuous long-time treatment can be performed. By providing the heating and drying device 4 in this configuration, shellfish can be reliably processed in continuous operation. Furthermore, by providing the bagging device 7, the obtained calcium oxide O5 can be stored in a good state.

(2)前記いずれかの貝類処理システムにおいて、抵抗型電気炉5の炉室51の平面視円形経路の円内または円外の下方に、炉室51から排出された酸化カルシウムO5を収集して収集状態で冷却する冷却貯留ホッパー6を具備し、この冷却貯留ホッパー6にて貯留した酸化カルシウムO5を常温にまで冷却することが好ましい。   (2) In any one of the shell processing systems described above, the calcium oxide O5 discharged from the furnace chamber 51 is collected below or inside the circle of the circular path in plan view of the furnace chamber 51 of the resistance electric furnace 5. It is preferable to provide a cooling storage hopper 6 that cools in the collected state, and cool the calcium oxide O5 stored in the cooling storage hopper 6 to room temperature.

炉室51の下方の円形経路の内部又は外部のいずれかに冷却貯留ホッパー6を設けることで、抵抗型電気炉5での熱処理によって得られた酸化カルシウムO5を冷却するまでの装置群をコンパクトに構成することができる。なお後述の実施例では平面視内部中央位置に冷却貯留ホッパー6を設けて抵抗型電気炉5と共にコンパクトに構成しているが、配置によっては平面視円外の位置に設けてもよい。   By providing the cooling storage hopper 6 either inside or outside the circular path below the furnace chamber 51, the apparatus group until the calcium oxide O5 obtained by the heat treatment in the resistance electric furnace 5 is cooled can be made compact. Can be configured. In the embodiment described later, the cooling storage hopper 6 is provided at the center position in the plan view and is configured compactly together with the resistance electric furnace 5, but it may be provided at a position outside the circle in the plan view depending on the arrangement.

(3)前記貝類処理システムにおいて、
抵抗型電気炉5が、耐熱炉材を主構成材とする耐火煉瓦からなる炉室51と、多数の基盤プレート520がコンベア連結された移動床式の平面視円形経路の基盤52と、基盤52を動力牽引して、炉室51内を基盤52の円形経路に沿って移動させる牽引手段とを具備することが好ましい。この場合、各基盤プレート520は図3に示すような部分円弧の両側縁と直線縁とで囲まれた形状となり、複数枚が直線縁にて互いに密着して隣り合うことで、平面視円形経路を構成する。なお真円に限らず、楕円、長円或いはこれらの扁平形状としてもよい。
(3) In the shellfish processing system,
The resistance electric furnace 5 includes a furnace chamber 51 made of a refractory brick mainly composed of a heat-resistant furnace material, a base 52 having a circular path in plan view of a moving floor type in which a large number of base plates 520 are conveyor-connected, and a base 52 It is preferable to provide traction means for moving the furnace chamber 51 along the circular path of the base 52 by power traction. In this case, each base plate 520 has a shape surrounded by both side edges and straight edges of the partial arc as shown in FIG. 3, and a plurality of sheets are in close contact with each other at the straight edges, so that a circular path in plan view Configure. The shape is not limited to a perfect circle, and may be an ellipse, an ellipse, or a flat shape thereof.

(4)前記いずれかの貝類処理システムの抵抗型電気炉5において、炉室51及び基盤52が共に耐熱炉材を主構成材とする耐火煉瓦からなることが好ましい。これらを共に耐火煉瓦で構成することで加熱効率が向上し、また移動床式炉として長時間の連続運転が可能なものとなる。特に耐火煉瓦からなる細幅の基盤プレート520を複数個、上面が載置面となるようにコンベア連結して平面視真円形経路を構成することで、加熱効率の良い炉床をコンパクトに構成することが出来る。   (4) In the resistance type electric furnace 5 of any one of the above shellfish processing systems, it is preferable that both the furnace chamber 51 and the base 52 are made of refractory bricks mainly composed of a heat-resistant furnace material. By configuring both of these with refractory bricks, the heating efficiency is improved and the moving bed furnace can be operated continuously for a long time. In particular, a hearth with good heating efficiency can be configured in a compact manner by connecting a plurality of narrow base plates 520 made of refractory bricks to form a circular path in plan view by connecting a plurality of base plates 520 so that the upper surface is a mounting surface. I can do it.

(5)前記貝類処理システムにおいて、粗砕装置3は、表面に複数の突起部がそれぞれ固設された一対または複数対のローラーを各対にて並行軸状に配置してなり、各ローラーを回転駆動させながら、各対のローラー間に脱塩貝類を通すことで、所定以下の大きさに粗砕すると共に、脱塩貝類に付着した水分を落とすことが好ましい。   (5) In the shellfish processing system, the crushing apparatus 3 is configured by arranging a pair or a plurality of rollers each having a plurality of protrusions fixed on the surface thereof in parallel shafts in each pair. While rotating, it is preferable to pass the desalted shellfish between each pair of rollers so as to roughly pulverize them to a predetermined size or less and to remove the moisture attached to the desalted shellfish.

(6)前記いずれかの貝類処理システムにおいて、袋詰め装置7は、
収容袋Pの口部を一枚ずつ引き上げる引き上げ手段71と、
引き上げた収容袋Pの口部内で水平の環状に広がることで、収容袋を開口した状態で吊下げ保持する帯板状の開口保持手段72と、
開口保持手段で開口した収容袋内に、粉状の酸化カルシウムO5を供給する供給手段と、
複数の開口保持手段を収容袋と共につり下げたまま運搬する運搬手段74と、
収容後の収容袋の口部の両外側に対向して一対設けられた水平棒状体のシーラー75とを具備してなる。
そして、シーラー75は、酸化カルシウムO5収容後の収容袋Pの口部を袋内の開口保持手段72と共に外側の対向両面から押しつぶして閉口させ、開口保持手段72を抜き取ったのちに加熱して収容袋Pを密閉するものであることが好ましい。
(6) In any one of the shellfish processing systems, the bagging device 7 includes:
A lifting means 71 for pulling up the mouth of the containing bag P one by one;
A band-plate-shaped opening holding means 72 that suspends and holds the storage bag in an open state by spreading in a horizontal annular shape in the mouth portion of the storage bag P that has been lifted,
Supply means for supplying powdered calcium oxide O5 into the containing bag opened by the opening holding means;
Conveying means 74 for conveying a plurality of opening holding means while being suspended together with the containing bag;
A pair of horizontal sticker sealers 75 are provided so as to face both outer sides of the mouth portion of the storage bag after storage.
The sealer 75 then closes the mouth portion of the containing bag P after containing the calcium oxide O5 together with the opening holding means 72 in the bag from both sides facing the outside, and after removing the opening holding means 72, heats and stores it. It is preferable that the bag P be sealed.

後述の実施例では、供給手段として上部から押し出して落下させる供給手段73を採用しているが、この構成に限らず種々の機構を採用することができる。   In the embodiment described later, the supply means 73 that is pushed out from the upper part and dropped is used as the supply means.

(7)前記いずれかの貝類処理システムにおいて、脱塩洗浄装置1は、
上部の拡径した投入口から海水つきの貝類を収容し、下部の縮径した排出口から排出する縦型筒状の原料ホッパー11と、
原料ホッパー11の下方にて下連通部101に連通し、この下連通部から斜め上方へ伸長する筒状容体10と、
筒状容体の伸長方向に沿って軸設された回転軸周りにらせん状に連続形成され、回転駆動によって貝類を軸方向に運搬するスクリュー羽根12と、
筒状容体内の下連通部よりも上方の天井部に配置されて内部に洗浄水を噴射する複数の噴射ノズル13を備えてなる。
そして筒状容体10は、下連通部よりも下方の底部に設けられ、筒状容体内の水を排出する排水口103と、筒状容体内の上方伸長先の底部に設けられ、容体内の貝類を外部へ排給する排給口104とを備える。
これらは、排水口103からの排水量の自動調整によって、噴射ノズル13から噴射された洗浄水量を所定範囲内に保つことで容体内に洗浄水Wを一定水位で貯留保持するものである。
そして、原料ホッパー11から供給された海水つきの貝類を筒状容体10内に貯留した洗浄水W内に浸漬させてスクリュー羽根12によって転回させながら伸長方向上方へ運搬し、この運搬した浸漬後の貝類を、洗浄水の水面上方にてスクリュー羽根12によって転回させながら噴射ノズル13によって洗浄したのちに、排給口104から外部へ排給することで貝類を脱塩することが好ましい。
(7) In any one of the shellfish processing systems, the desalting / cleaning apparatus 1 includes:
A vertical cylindrical raw material hopper 11 that accommodates shellfish with seawater from the upper diameter inlet, and discharges it from the lower diameter outlet;
A cylindrical container 10 that communicates with the lower communication portion 101 below the raw material hopper 11 and extends obliquely upward from the lower communication portion;
A screw blade 12 that is continuously formed in a spiral around a rotation axis that is provided along the extending direction of the cylindrical container, and that conveys shellfish in the axial direction by rotational driving;
It has a plurality of injection nozzles 13 which are arranged in a ceiling part above the lower communication part of the cylindrical container and inject cleaning water into the inside.
The cylindrical container 10 is provided at a bottom portion below the lower communication portion, and is provided at a drain port 103 for discharging water in the cylindrical container, and at a bottom portion of an upper extension destination in the cylindrical container. And a discharge port 104 for discharging shellfish to the outside.
In these cases, the cleaning water W is stored and held at a constant water level in the container by keeping the amount of cleaning water sprayed from the spray nozzle 13 within a predetermined range by automatically adjusting the amount of drainage from the drain outlet 103.
Then, the shellfish with seawater supplied from the raw material hopper 11 is immersed in the washing water W stored in the cylindrical container 10 and conveyed upward in the extension direction while being rotated by the screw blades 12, and the conveyed shellfish after immersion. It is preferable that the shellfish be desalted by being discharged from the discharge port 104 to the outside after being washed by the spray nozzle 13 while being rotated by the screw blade 12 above the surface of the washing water.

(8)前記(7)の貝類処理システムにおいて、スクリュー羽根12には、回転軸方向に隣り合う羽根板間をつなぐ連接板121が、回転軸周りに等間隔に複数枚固設されてなり、各連接板121は、回転軸方向に対して軸側面視及び軸断面視の両方で傾斜して、いわゆるねじれ角度で配置された平板であることが好ましい。   (8) In the shell processing system of (7), the screw blades 12 are each provided with a plurality of connecting plates 121 that connect between blade plates adjacent to each other in the rotation axis direction, and are fixed at equal intervals around the rotation axis. Each connecting plate 121 is preferably a flat plate that is inclined at both the axial side view and the axial sectional view with respect to the rotation axis direction and is arranged at a so-called twist angle.

本考案の貝類処理システムは上記手段を講じており、抵抗型の移動床式炉と、その前処理である脱塩、乾燥、小砕片化のための各種装置と、後処理である袋詰め装置7とを、対象物の相互運搬を可能としてすべて備えることで、長時間の連続的な自動運転が可能となっている。これより、酸化カルシウムO5を連続生産することが可能である。   The shell processing system of the present invention has the above-mentioned means, a resistance type moving bed furnace, various devices for desalination, drying and fragmentation as pre-treatment thereof, and a bagging device as post-treatment. 7 is provided so that the objects can be mutually transported, enabling continuous automatic operation for a long time. Thus, it is possible to continuously produce calcium oxide O5.

また移動床式の抵抗型電気炉5であるから、炉の運転にCOの排出を伴わず、火力調整等の運転管理が不要となり、また長時間運転に耐えうるという耐久性の課題に対応したものとなっている。 In addition, because it is a moving-bed type resistance electric furnace 5, it does not involve CO 2 emissions during operation of the furnace, eliminates the need for operation management such as thermal power adjustment, and addresses durability issues such that it can withstand long-term operation. It has become.

本貝類処理システムの実施例の全体構成を示した説明図。Explanatory drawing which showed the whole structure of the Example of this shellfish processing system. 本貝類処理システムの実施例の脱塩洗浄装置1、脱塩物貯留ホッパー2及び粗砕装置3を示した側面視説明図。Side view explanatory drawing which showed the desalting washing | cleaning apparatus 1, the desalted substance storage hopper 2, and the crushing apparatus 3 of the Example of this shellfish processing system. 本貝類処理システムの実施例の抵抗型電気炉5及び冷却貯留ホッパー6を示した斜視説明図。The perspective explanatory view showing resistance type electric furnace 5 and cooling storage hopper 6 of the example of this shellfish processing system. 本貝類処理システムの実施例の加熱乾燥装置4、抵抗型電気炉5、冷却貯留ホッパー6、及び袋詰め装置7を示した側面視説明図。Side view explanatory drawing which showed the heating drying apparatus 4, the resistance-type electric furnace 5, the cooling storage hopper 6, and the bagging apparatus 7 of the Example of this shellfish processing system.

以下、本貝類処理システムの実施形態を、実施例として示す各図と共に説明する。     Hereinafter, an embodiment of the shellfish processing system will be described with each drawing shown as an example.

実施例の貝類処理システムは、海産の貝類又は介類を連続的に処理して酸化カルシウムO5を生産する貝類処理システムであって、基本的に下記構成からなる(図1)。
・貝類に付着する塩類を水洗によって除去して脱塩貝類を得る脱塩洗浄装置1
・脱塩貝類を貯留する脱塩物貯留ホッパー2
・脱塩貝類を粗砕して粗砕片を得る粗砕装置3
・粗砕片を500℃〜600℃で加熱乾燥させて半焼成片を得る加熱乾燥装置4(前処理装置)
・半焼成片を平面視円形経路であって内部温度1,000℃〜1,600℃の炉室内の移動床式の基盤上を通過させて焼成し、酸化カルシウムO5を得ると共にそれ以外の構成材を焼却する抵抗型電気炉5(本炉)
・酸化カルシウムO5を貯留しながら冷却する冷却貯留ホッパー6
・酸化カルシウムO5を収集して収容袋内に密封する袋詰め装置7
(本貝類処理システムの実施例の主なポイント)
本貝類処理システムは、貝類或いは介類を原料とした原料処分システム兼、酸化カルシウムO5を得るシステムであり、貝類の最終処分方法として、抵抗型の電気加熱炉による1000℃以上の連続的な熱処理(焼成)を行い、酸化カルシウムO5に変化させることがポイントとなっている。貝類は1000℃以上の高温で焼く事により物性が酸化カルシウムO5に変化する。
The shellfish processing system of an Example is a shellfish processing system which processes the marine shellfish or shellfish continuously, and produces calcium oxide O5, Comprising: Basically, it consists of the following structures (FIG. 1).
・ Desalination and washing device 1 to obtain salted shellfish by removing salt adhering to shellfish with water
・ Desalinated salt storage hopper 2 for storing desalted shellfish
・ Crushing device 3 to crush demineralized shellfish to obtain coarse fragments
-Heat drying device 4 (pretreatment device) that heat-drys coarsely crushed pieces at 500 ° C to 600 ° C to obtain semi-fired pieces
-The semi-fired piece is fired by passing through a moving bed type base in a furnace chamber having an internal temperature of 1,000 ° C to 1,600 ° C in a circular path in plan view to obtain calcium oxide O5 and other configurations Resistance electric furnace 5 (main furnace) for incinerating materials
-Cooling storage hopper 6 that cools while storing calcium oxide O5
A bagging device 7 that collects calcium oxide O5 and seals it in the containing bag
(Main points of the embodiment of this shellfish processing system)
This shellfish processing system is a raw material disposal system that uses shellfish or shellfish as a raw material, and is a system for obtaining calcium oxide O5. As a final disposal method for shellfish, continuous heat treatment at 1000 ° C. or more by a resistance type electric heating furnace The point is to perform (firing) and change to calcium oxide O5. Shellfish are changed to calcium oxide O5 by baking at a high temperature of 1000 ° C. or higher.

最終的に得た酸化カルシウムO5はそのまま利用することも出来、何かを添加する事により又その物性を変化させ原材料として利用することや、自然に戻すなり副産物として再利用することができる。   The calcium oxide O5 finally obtained can be used as it is, and can be reused as a by-product as it is returned to nature or used as a raw material by adding something or changing its physical properties.

また、抵抗型電気炉5による連続熱処理を効率的に行うための脱塩洗浄装置1、粗砕装置3、加熱乾燥装置4を順に前処理装置群としてひとつのプラント内に備え、これら装置による脱塩工程、粗砕工程、前処理用の加熱乾燥工程を順に行ってから本炉である抵抗型電気炉5による熱処理を行うことがポイントのひとつとなっている。   In addition, a desalting and cleaning device 1, a crushing device 3, and a heating and drying device 4 for efficiently performing continuous heat treatment in the resistance electric furnace 5 are sequentially provided in a single plant as a pretreatment device group. One of the points is to perform the heat treatment by the resistance electric furnace 5 which is the main furnace after sequentially performing the salt process, the coarse crushing process, and the heat drying process for pretreatment.

さらに袋詰め装置7を一プラント内にすべて備え、これらを順に運搬コンベアCでつなぐことで温度・含水率制御を行いながら一連の生産システムを形成したことが新規なポイントとなっている。   Furthermore, it is a new point that all the bagging devices 7 are provided in one plant, and a series of production systems are formed while controlling the temperature and moisture content by sequentially connecting them with a conveyor C.

特に本炉として、複雑な設備が必要とならない抵抗型電気炉5を用いており、炉内では対象物が円形経路の可動床(基盤)上を移動することで、長時間の連続運転を容易に行うことができる点、酸化カルシウムO5を連続的に得ることができる点で新規となっている。   In particular, a resistance electric furnace 5 that does not require complicated equipment is used as the main furnace, and the object moves on a movable floor (base) in a circular path so that it can be operated continuously for a long time. It is novel in that it can be performed continuously and calcium oxide O5 can be obtained continuously.

(脱塩洗浄装置1)
脱塩洗浄装置1は、表面または内部の塩類を水洗いによって除去する(脱塩する)装置であり、本装置によって脱塩洗浄工程を行う。本装置は具体的には図2に示すように、
上部の拡径した投入口から海水つきの貝類(原料貝類O1)を収容して下部の縮径した排出口から排出する縦型筒状の原料ホッパー11と、
原料ホッパー11の下方にて下連通部101に連通し、この下連通部から円筒状の内部空間を有して斜め上方へ伸長する筒状容体10と、
筒状容体10内に軸設された駆動軸12S周りにらせん状に連続形成され、駆動軸12Sの回転駆動によって貝類を軸方向に沿って斜め上方へ運搬するスクリュー羽根12と、
筒状容体内の下連通部よりも上方の天井部に配置されて内部に洗浄水を噴射する複数の噴射ノズル13を備える。
(Desalination washing device 1)
The desalting washing apparatus 1 is an apparatus for removing (desalting) salt on the surface or inside by washing with water, and performs a desalting washing process by this apparatus. Specifically, as shown in FIG.
A vertical cylindrical raw material hopper 11 that accommodates shellfish with seawater (raw material shellfish O1) from the upper diameter inlet and discharges from the lower diameter outlet;
A cylindrical container 10 that communicates with the lower communication portion 101 below the raw material hopper 11 and that extends obliquely upward from the lower communication portion with a cylindrical internal space;
A screw blade 12 continuously formed in a spiral around a drive shaft 12S provided in the cylindrical container 10 and carrying shells obliquely upward along the axial direction by rotational drive of the drive shaft 12S;
A plurality of injection nozzles 13 that are disposed in a ceiling portion above the lower communication portion of the cylindrical container and inject cleaning water therein are provided.

筒状容体10は、原料ホッパー11の下方にて下連通部101に連通し、この下連通部から円筒状の内部空間を有して斜め上方へ伸長する。伸長方向の両端付近にはそれぞれ閉塞壁102が形成され、両端の閉塞壁102間によって、内部に洗浄水及び原料貝類O1を保持しうる円筒状の内部空間が形成される。なお閉塞壁102は中央に駆動軸12Sが貫通する貫通孔が形成され、貫通孔には駆動軸12Sを回転自在に支持するためのベアリング構造が設けられている。   The cylindrical container 10 communicates with the lower communication portion 101 below the raw material hopper 11, and extends obliquely upward from the lower communication portion with a cylindrical internal space. Closed walls 102 are formed in the vicinity of both ends in the extending direction, and a cylindrical internal space is formed between the closed walls 102 at both ends so that the washing water and the raw shellfish O1 can be held therein. The blocking wall 102 is formed with a through-hole through which the drive shaft 12S passes in the center, and a bearing structure for rotatably supporting the drive shaft 12S is provided in the through-hole.

また筒状容体10は、下連通部101よりも下方の底部に設けられ、筒状容体10内の水を排出する排水口103と、筒状容体10内の上方伸長先の底部に設けられ、容体内の貝類を外部へ排給する排給口104とを備える。   The cylindrical container 10 is provided at the bottom below the lower communication portion 101, and is provided at the drainage port 103 for discharging the water in the cylindrical container 10 and the bottom of the upper extension destination in the cylindrical container 10, And a discharge port 104 for discharging shellfish in the container to the outside.

中でも下側の閉塞壁102で仕切られた内部空間よりも下方先側に底部が設けられており、下側の閉塞壁102と底部との間に、洗浄後の水を排水するための円筒状の排水室が形成される。排水口103は、この排水室の側部に設けられると共に、排水量を自動調整するための排水バルブが介設されている。排水室には下側の閉塞壁102の貫通孔から洗浄水が流入し、この室内で原料貝類O1を除く洗浄水を一端貯水してから排水する。この排水室への貯水および排水口103からの排水量の自動調整によって、噴射ノズル13から噴射された洗浄水量を所定範囲内に保つことで容体内に洗浄水Wを一定水位で貯留保持している。   In particular, a bottom portion is provided on the lower side of the inner space partitioned by the lower blocking wall 102, and a cylindrical shape for draining water after washing between the lower blocking wall 102 and the bottom portion. A drainage chamber is formed. The drainage port 103 is provided at the side of the drainage chamber, and a drainage valve for automatically adjusting the amount of drainage is interposed. Wash water flows into the drainage chamber from the through hole of the lower blocking wall 102, and the wash water excluding the raw material shells O1 is stored in the chamber and then drained. By automatically adjusting the amount of water stored in the drainage chamber and the amount of drainage from the drainage port 103, the amount of cleaning water sprayed from the spray nozzle 13 is kept within a predetermined range, so that the cleaning water W is stored and held at a constant water level in the container. .

駆動軸12Sは、筒状容体10内であって円筒状の内部空間の断面視中央位置にて、モーター105によって両方向に回転駆動可能に軸設される。   The drive shaft 12S is installed in the cylindrical container 10 so as to be rotationally driven in both directions by the motor 105 at a central position in a sectional view of the cylindrical internal space.

(スクリュー羽根12)
スクリュー羽根12は、駆動軸12S周りにらせん状に連なって形成された羽根板からなる。この羽根板は、軸端部から見て同一の円形に重なり、軸方向に略等間隔に離間して連なると共に、一定曲率のねじれ変形によって一体的に形成される。
(Screw blade 12)
The screw blade 12 includes a blade plate formed in a spiral manner around the drive shaft 12S. The slats overlap in the same circle as viewed from the shaft end, and are continuously spaced apart at substantially equal intervals in the axial direction, and are integrally formed by torsional deformation with a constant curvature.

(連接板121)
スクリュー羽根12には、回転軸方向に隣り合う羽根板間をつなぐ連接板121が、回転軸周りに等間隔に複数枚、略放射状に固設される。各連接板121は、回転軸12Sの伸張方向に対して軸側面視及び軸断面視の両方で傾斜した、いわゆるねじれ角度で配置された平板である。連接板121によって貝類の転回を促し、洗浄水が裏側にまで行き渡るようにしている。スクリュー羽根12は駆動軸12Sの回転駆動によって原料貝類O1を転回させながら軸方向に沿って斜め上方へ運搬するが、このとき連接板121によって原料貝類O1をより多く転回させ、より確実に上方運搬するものとしている。
(Connecting plate 121)
A plurality of connecting plates 121 that connect between blade plates adjacent to each other in the rotation axis direction are fixed to the screw blades 12 in a substantially radial manner around the rotation axis at equal intervals. Each connecting plate 121 is a flat plate disposed at a so-called twist angle that is inclined in both the axial side view and the axial sectional view with respect to the extending direction of the rotating shaft 12S. The connecting plate 121 urges the shells to turn so that the washing water can reach the back side. The screw blade 12 conveys the raw shellfish O1 obliquely upward along the axial direction while rotating the raw shellfish O1 by the rotational drive of the drive shaft 12S. At this time, the connecting shell 121 rotates the raw shellfish O1 more and more reliably conveys upward. I am going to do it.

そして、原料ホッパー11から供給された海水つきの原料貝類O1を筒状容体10内は、噴射ノズル13によって常時注水されるとともに必要に応じて排水バルブを有した排水口103によって適宜排水され、これによって内部空間に洗浄水Wが常に一定範囲量となっている。この洗浄水Wは原料貝類O1を一定時間浸漬させる。   Then, the raw material shellfish O1 with seawater supplied from the raw material hopper 11 is constantly poured into the cylindrical container 10 by the injection nozzle 13 and drained as appropriate by the drainage port 103 having a drainage valve as required. The washing water W is always in a certain range in the internal space. This washing water W immerses the raw shellfish O1 for a certain time.

噴射ノズル13は、洗浄水Wに浸漬され、伸長方向上方へ運搬されてきた原料貝類O1に、洗浄水の水面上方にて洗浄水Wを噴射するものである。スクリュー羽根12によって転回させた状態のまま洗浄することで、より効率的な脱塩洗浄を行うものとなっている。   The spray nozzle 13 sprays the cleaning water W above the surface of the cleaning water onto the raw material shells O1 that has been immersed in the cleaning water W and carried upward in the extending direction. By performing the cleaning while being rotated by the screw blade 12, more efficient desalting cleaning is performed.

(第一コンベアC1)
第一コンベアC1は、脱塩洗浄装置1と脱塩物貯留ホッパー2の間に設けられ、洗浄貝類O2を上方位置まで運搬する。具体的には図2に示すように、配給口104の下方に設置され、そこから緩やかな勾配で上方に傾斜する第一コンベアCaと、急勾配で上方に傾斜すると共に運搬物の落下防止用爪が等間隔に設けられた第二コンベアCbと、原料ホッパー6内に投入する略水平の第三コンベアCcとから構成され、これら第一コンベアCa、第二コンベアCb、第三コンベアCcの順に、脱塩洗浄後の洗浄貝類O2を連続して上方の脱塩物貯留ホッパー2まで運搬する。またこれらの上方運搬によって脱塩貝類O2の水分を落下させる。
(First conveyor C1)
The 1st conveyor C1 is provided between the desalting washing | cleaning apparatus 1 and the desalination thing storage hopper 2, and conveys the washing shellfish O2 to an upper position. Specifically, as shown in FIG. 2, the first conveyor Ca is installed below the distribution port 104, and is inclined upward with a gentle gradient therefrom. Consists of a second conveyor Cb with claws provided at equal intervals and a substantially horizontal third conveyor Cc that is put into the raw material hopper 6. The first conveyor Ca, the second conveyor Cb, and the third conveyor Cc in this order. Then, the washed shellfish O2 after the desalting washing is continuously transported to the upper desalted substance storage hopper 2. Moreover, the water | moisture content of demineralized shellfish O2 is dropped by these upward conveyance.

(脱塩物貯留ホッパー2)
脱塩物貯留ホッパー2は、脱塩装置で脱塩した脱塩貝類O2を貯留して、これ以降の処理量を調整するものである。脱塩貝類O2は、円筒状の取り込み口21から本体内に取り込まれ、内部に貯留される。すり鉢状の本体下部のすり鉢状の底に設けられた排出ノズル23から、排出バルブ22を介して所定量ずつ排出される。
(Desalinated matter storage hopper 2)
The desalted substance storage hopper 2 stores desalted shellfish O2 desalted by the desalting apparatus and adjusts the subsequent processing amount. The desalted shellfish O2 is taken into the main body from the cylindrical intake 21 and stored therein. A predetermined amount is discharged through a discharge valve 22 from a discharge nozzle 23 provided at the bottom of the mortar-shaped bottom of the mortar-shaped main body.

(粗砕装置3)
粗砕装置3は、脱塩貝類O2を一定以内の大きさに粗砕して、所定以下の大きさであって大きな突起部のない安定した形状の粗砕片O3を得るものであり、本装置によって粗砕工程を行う。所定以下の最大長の粗砕片O3とすることにより、本炉である抵抗型電気炉5における熱効率を高め、連続処理を行うことができる。粗砕片O3は例えば、最大長2cmm前後、大きくとも最大長4〜5cmの粗粒状に揃えられて本装置から排出される。これにより、加熱乾燥装置4や抵抗型電気炉5での移動床運搬中に、炉内で破裂、崩落、或いは倒落したり、これらによって基盤プレートの隙間に挟まったりするのを防ぐことができる。また粗砕装置3内を通って砕かれる際に、水洗脱塩後の貝類の大半の水分を落とすものとなっている。
(Crushing device 3)
The crushing device 3 is a device for crushing the demineralized shellfish O2 to a size within a certain range to obtain a roughly shaped fragment O3 having a size smaller than a predetermined size and having no large protrusions. The crushing process is carried out. By setting it as the coarse fragment O3 of the maximum length below predetermined, the thermal efficiency in the resistance type electric furnace 5 which is a main furnace can be improved, and a continuous process can be performed. The coarsely crushed pieces O3 are, for example, arranged in coarse particles having a maximum length of around 2 cm and a maximum length of 4 to 5 cm and are discharged from the apparatus. Thereby, it is possible to prevent rupture, collapse, or fall in the furnace during transportation of the moving bed in the heating / drying apparatus 4 or the resistance electric furnace 5, or the occurrence of being caught in the gap between the base plates. In addition, when crushed through the crushing apparatus 3, most of the water of the shellfish after washing and desalting is removed.

具体的には図2に示すように、水平軸の横置き円柱からなる一対または複数対のローラー32を、各対にて並行軸となるように設置し、1つのモーター33によってそれぞれ逆方向に回転駆動させて使用する。下方に縮径した錐体状の投入枠31から、駆動中の一対のローラー32間に脱塩貝類O2を投入して挟み、ローラー32間の下部から粗砕片O3を排出する。各ローラー32の柱状表面にはそれぞれ、放射方向を頂部とする錘状の突起が前面に亘ってランダムに固設されており、両側からこの突起で挟みこむことによって、貝類は確実に一定以下の大きさにまで粗砕される。   Specifically, as shown in FIG. 2, a pair or a plurality of pairs of rollers 32 composed of horizontal horizontal cylinders are installed so as to be parallel axes in each pair, and each motor 33 reverses in the opposite direction. Used by rotating. The demineralized shellfish O2 is put between a pair of driven rollers 32 from a cone-shaped throwing frame 31 having a diameter reduced downward, and the coarsely broken pieces O3 are discharged from the lower part between the rollers 32. Each columnar surface of each roller 32 has a weight-like projection with the radial direction at the top, which is randomly fixed over the front surface. By sandwiching the projections from both sides, the shells are surely below a certain level. Crush to size.

(加熱乾燥装置4)
加熱乾燥装置4は、前処理として粗砕片を加熱乾燥させて半焼成片を得る前処理用装置である。
(Heat drying device 4)
The heat drying apparatus 4 is a pretreatment apparatus that obtains a semi-fired piece by heating and drying coarse crushed pieces as a pretreatment.

(第二コンベアC2、第三コンベアC3)
第二コンベアC2は粗砕装置3と加熱乾燥装置4の間に設けられ、粗砕片O3を水平運搬する。第三コンベアC3は加熱乾燥装置4と抵抗型電気炉5の間に設けられ、半焼成片を水平運搬する。また加熱乾燥装置4の炉内では、粗砕片O3を耐熱性の移動床によって運搬する。本システムではこれらの運搬経路を平面視直線状としている。なお、これらを同一のコンベアベルトによって形成しても良い。
(Second conveyor C2, third conveyor C3)
The second conveyor C2 is provided between the coarse crushing device 3 and the heating and drying device 4, and horizontally conveys the coarsely crushed pieces O3. The third conveyor C3 is provided between the heating and drying device 4 and the resistance electric furnace 5, and horizontally conveys the semi-fired pieces. Further, in the furnace of the heating and drying apparatus 4, the coarsely crushed pieces O3 are conveyed by a heat-resistant moving bed. In this system, these transport routes are linear in plan view. These may be formed by the same conveyor belt.

(抵抗型電気炉5)
しかして、本システムにおける本炉である抵抗型電気炉5は、焼却炉よりも処理温度が高く、溶融炉よりも処理温度が低い。これらの炉の中間に位置づけられる抵抗型電気炉5である。本装置は電気焼成工程を行う。
(Resistive electric furnace 5)
Therefore, the resistance electric furnace 5 which is a main furnace in the present system has a higher processing temperature than the incinerator and a lower processing temperature than the melting furnace. This is a resistance electric furnace 5 positioned between these furnaces. This apparatus performs an electric baking process.

抵抗型電気炉5の動作はオイルを使った燃焼でなく、電気炉を採用することによりCO2の削減に貢献出来る焼成炉となっている。炉はその目的によって多くのタイプと呼び名があり、一般的に言われるのは焼却炉、燃焼炉、高炉、溶解炉、溶融炉である。またエネルギー源は石油、ガス、電気、(原子力、風力、波力、火力、水力、太陽、)等に大別される。本処理システムの本炉として基本的に電気炉を採用しており、長時間にわたって自動運転することができる。   The operation of the resistance electric furnace 5 is not a combustion using oil but a firing furnace that can contribute to the reduction of CO2 by adopting an electric furnace. Furnaces are called many types depending on their purpose, and commonly called incinerators, combustion furnaces, blast furnaces, melting furnaces and melting furnaces. Energy sources are roughly divided into oil, gas, electricity, (nuclear power, wind power, wave power, thermal power, hydropower, sun, etc.). An electric furnace is basically adopted as the main furnace of this treatment system, and automatic operation can be performed for a long time.

電気炉そのものは電気ヒーターと耐熱炉材とを組み合わせた極めてシンプルな炉であって、複雑な装置が少なく部品点数が少ないのが特徴である。よって運転管理上メンテナンス等の維持管理が容易であり、作業の安全性や品質管理、行程、時間、人件費等、どの面から見ても経費削減に繋がる。また熱源を電気に求めているため、将来的なCO2 の削減目標など社会コストやオイルやガスを使用する焼却炉の維持費や産廃費用も含めたコストと比べればコスト削減に繋がる。日々多くの貝類を処理する為には処理能力からどうしても連続炉にする必要があり、又システムとして自動運転可能な炉であり可動式、運転温度能力は1000℃〜1600℃とし長時間運転に耐えうる構造が求められる為、機能として満たされたものである。   The electric furnace itself is an extremely simple furnace combining an electric heater and a heat-resistant furnace material, and is characterized by a small number of complicated devices and a small number of parts. Therefore, maintenance such as maintenance is easy in terms of operation management, and it leads to cost reduction in all aspects such as work safety, quality control, process, time, and labor cost. Moreover, since the heat source is demanded for electricity, it will lead to cost reduction compared to social costs such as future CO2 reduction targets, and costs including maintenance costs and industrial waste costs for incinerators using oil and gas. In order to treat many shellfish every day, it is absolutely necessary to use a continuous furnace because of its processing capacity, and it is a furnace that can be operated automatically as a system. It is movable and has an operating temperature capacity of 1000 ° C to 1600 ° C to withstand long-term operation. Since a possible structure is required, it is fulfilled as a function.

炉の形状は平面視円形経路状の基盤52の両側壁部と天井部を覆って炉室51が形成され、この炉室51内で半焼成片O4が円形経路に沿って移動する仕組みとなっている。貝類の焼成炉として平面視真円形状の移動床式の炉体であり、連続運転可能な抵抗型の電気炉として構成することで、均等に加熱処理を行うとともに連続的な処理を可能としている。   The shape of the furnace is such that a furnace chamber 51 is formed so as to cover both side walls and the ceiling of the base 52 having a circular path shape in plan view, and the semi-fired piece O4 moves along the circular path in the furnace chamber 51. ing. It is a moving bed type furnace body with a perfect circular shape in plan view as a shell firing furnace, and is configured as a resistance-type electric furnace that can be operated continuously, enabling uniform heat treatment and continuous treatment. .

(抵抗型電気炉5の具体的構成)
抵抗型電気炉5は図3に示すように、半焼成片O4を投入する投入管50と、投入管50に一端付近の天井部で連結され、所定の平面経路状に形成された炉室51と、多数の基盤プレート520がコンベア状に連結されて前記所定の平面経路状に形成された基盤52と、対象物を載置した基盤52を動力牽引して炉室内を所定の経路状に水平移動させる牽引手段とを具備する。炉室51及び基盤52は共に、耐熱炉材を主構成材とする耐火煉瓦からなる。
(Specific configuration of resistance type electric furnace 5)
As shown in FIG. 3, the resistance electric furnace 5 is connected to a charging pipe 50 into which a semi-fired piece O4 is charged, and a furnace chamber 51 connected to the charging pipe 50 at a ceiling near one end and formed in a predetermined planar path shape. And a plurality of base plates 520 connected in a conveyor shape to form the predetermined plane path, and the base 52 on which the object is placed is powered to pull the furnace chamber horizontally in the predetermined path. Traction means for movement. Both the furnace chamber 51 and the base 52 are made of refractory bricks mainly composed of a heat-resistant furnace material.

(炉室51)
炉室51は基盤52の両側面及び天井面の周囲三面を覆う。基端側の天井に設けられた上部接続口501から排出板54の手前部分の排出口5hまで、基盤52に沿って平面視円形状に伸びる。炉室51は排出板54の部分のみ区切られた部分円形状となっており、先端が排出口5hとなっている。
(Furnace chamber 51)
The furnace chamber 51 covers both sides of the base 52 and the three surrounding surfaces of the ceiling surface. From the upper connection port 501 provided in the base end side ceiling to the discharge port 5h in the front part of the discharge plate 54, it extends in a circular shape in plan view along the base 52. The furnace chamber 51 has a partial circular shape in which only the portion of the discharge plate 54 is divided, and the tip is a discharge port 5h.

排出板54は水平に配置された円柱状の軸体周りに等間隔に複数枚が放射固定される。軸体は間欠時間ごとに回転することで、焼成後の酸化カルシウムO5を平面視円形経路よりも平面視内側の排出口5h内に払い落とす。   A plurality of discharge plates 54 are fixed by radiation around a cylindrical shaft body arranged horizontally at equal intervals. By rotating the shaft body every intermittent time, the calcined calcium oxide O5 is wiped down into the discharge port 5h on the inner side in the plan view than the circular route in the plan view.

(牽引手段)
牽引手段は、半焼成片の入口部である上部接続口501付近から出口部である排出口5hまで、基盤52上の半焼成片を、時間をかけて円形経路に沿って移動(周回移動)させる。平面視円形経路状に移動させ、経路方向の変化に伴って配置角度を変えながら焼成させることで、対象物の周囲を均等に加熱して酸化カルシウムO5を確実に得る。
(Traction means)
The pulling means moves the semi-fired piece on the base 52 along the circular path over time from the vicinity of the upper connection port 501 that is the entrance part of the semi-fired piece to the discharge port 5h that is the exit part (circular movement). Let By moving in a circular path shape in plan view and firing while changing the arrangement angle according to the change in the path direction, the periphery of the object is heated evenly, and calcium oxide O5 is reliably obtained.

(炉内温度の変更と速度調整)
抵抗型電気炉5は、電圧変位によって炉内温度を1000℃〜1500℃の間で調節する温度調節手段と、牽引手段の牽引速度を調節する牽引速度調節手段とを具備している。これら2手段を適宜組み合わせて使用する。温度調節手段による炉内温度の変更と、牽引速度調節手段による速度の変更とを組み合わせると、抵抗型電気炉5の処理能力に幅を持たせることができる。
炉室51から排出された酸化カルシウムO5は抵抗型電気炉5の平面視円形経路の炉室51の円形中央位置下方に設けられた、すり鉢状の収集器54によって収集される。収集器54は最下部が開口され、下方の冷却貯留ホッパー6にパイプ連結される。
(Changing furnace temperature and speed adjustment)
The resistance electric furnace 5 includes temperature adjusting means for adjusting the furnace temperature between 1000 ° C. and 1500 ° C. by voltage displacement, and traction speed adjusting means for adjusting the traction speed of the traction means. These two means are used in appropriate combination. By combining the change in the furnace temperature by the temperature adjusting means and the change in the speed by the traction speed adjusting means, the processing capability of the resistance electric furnace 5 can be widened.
Calcium oxide O5 discharged from the furnace chamber 51 is collected by a mortar-shaped collector 54 provided below the circular center position of the furnace chamber 51 in a circular path in plan view of the resistance electric furnace 5. The collector 54 is open at the bottom and is piped to the cooling storage hopper 6 below.

(冷却貯留ホッパー6)
冷却貯留ホッパー6は、収集器53から連結パイプC5によってパイプ連結されると共に天井を有して略密閉された粉貯留装置であって、本システムの抵抗型電気炉5までの工程で得られた酸化カルシウムO5を貯留しながら常温まで冷却する冷却貯留工程を行う。冷却貯留ホッパー6は具体的には図3に示すように、抵抗型電気炉5の平面視円形経路の円内または円外の下方に配置されており、縦型円筒形状の本体貯留部61と、冷却貯留ホッパー6の外部に設けられ、貯留部61の外側面に連通された冷却器62とを具備し、酸化カルシウムO5を本体貯留部61内に貯留しながら貯留部61内へ常に冷却風を拭き込んでいる。平面視円形経路の円内下方に配置され、図3のように抵抗型電気炉5と上下に一体的に配置されることでコンパクトに構成される。なお図3のように、本体貯留部61の内部には攪拌板63を備え、鉛直軸の攪拌板63によって内部攪拌しながら貯留するものとしてもよい。
(Cooling storage hopper 6)
The cold storage hopper 6 is a powder storage device that is pipe-connected from the collector 53 by a connection pipe C5 and has a ceiling and is substantially sealed, and is obtained in the process up to the resistance electric furnace 5 of the present system. A cooling and storing step of cooling to normal temperature while storing calcium oxide O5 is performed. Specifically, as shown in FIG. 3, the cooling storage hopper 6 is arranged in a circular path of the resistance-type electric furnace 5 in a circular path in a plan view or below the circle, and has a vertical cylindrical main body storage section 61. And a cooler 62 provided outside the cooling storage hopper 6 and communicated with the outer side surface of the storage unit 61, and always stores cooling air into the storage unit 61 while storing the calcium oxide O5 in the main body storage unit 61. Wipe off. It arrange | positions in the circle | round | yen downward of the circular path | route of planar view, and is comprised compactly by arrange | positioning integrally with the resistance type electric furnace 5 like FIG. As shown in FIG. 3, the main body storage unit 61 may be provided with a stirring plate 63 and stored while being stirred internally by the vertical axis stirring plate 63.

縦型円筒状の排出ノズル64には排出バルブ65が介設されており、排出バルブ65は、貯留部60への貯留量が所定値を超えたとき、かつ下方排出部64付近の貯留物が所定の温度以下になったときに自動的に開くものとしている。   A discharge valve 65 is interposed in the vertical cylindrical discharge nozzle 64, and the discharge valve 65 is configured to store a reservoir in the vicinity of the lower discharge section 64 when the storage amount in the storage section 60 exceeds a predetermined value. It automatically opens when the temperature falls below a predetermined temperature.

冷却貯留ホッパー6の側部上方よりの位置には、ファン及び熱交換器を内蔵した冷却器63がダクト連結されており、冷却器63で発生させた冷風をダクト連結部から吹き込むことによって、本体貯留部61内に貯留した酸化カルシウムO5を常温まで冷却する。貯留状態で常温まで冷却させることで、その後の袋詰め工程で収容袋Pが熱変性することなく、袋詰めを安全に行うことができる。   A cooler 63 containing a fan and a heat exchanger is duct-connected at a position above the side of the cooling storage hopper 6. The calcium oxide O5 stored in the storage unit 61 is cooled to room temperature. By cooling to room temperature in the storage state, the bag can be safely packed without the thermal denaturation of the storage bag P in the subsequent bag packing process.

(袋詰め装置7)
袋詰め装置7は、冷却貯留工程で貯留され、冷却された酸化カルシウムO5を所定量ずつ収容袋P内に袋詰めして運搬可能な状態とする装置であり、本装置によって袋詰め工程が行われる。図4に示すように収容袋Pの口部を一枚ずつ引き上げる引き上げ手段71と、引き上げた収容袋Pの口部内で水平の環状に広がることで、収容袋を開口した状態で吊下げ保持する帯板状の開口保持手段72と、開口保持手段で開口した収容袋内に、粉状の酸化カルシウムO5を上部から押し出して落下させる供給手段73と、複数の開口保持手段を収容袋と共につり下げたまま運搬する運搬手段74と、収容後の収容袋の口部の両外側に対向して一対設けられた水平棒状体のシーラー75とを具備してなり、
シーラー75は、酸化カルシウムO5収容後の収容袋Pの口部を袋内の開口保持手段72と共に外側の対向両面から押しつぶして閉口させ、開口保持手段72を抜き取ったのちに加熱して収容袋Pを密閉し、密閉袋P2とする。密閉袋P2は最終コンベアC6で運搬される。
(Bagging device 7)
The bagging device 7 is a device that packs a predetermined amount of the cooled calcium oxide O5 stored in the cooling and storing step into the containing bag P so that it can be transported. Is called. As shown in FIG. 4, the lifting means 71 for pulling up the mouth portion of the storage bag P one by one, and spreading horizontally in the mouth portion of the lifted storage bag P, the suspension bag is suspended and held open. A band-plate-shaped opening holding means 72, a supply means 73 for extruding and dropping powdered calcium oxide O5 from the upper part into the accommodation bag opened by the opening holding means, and a plurality of opening holding means suspended together with the accommodation bag A conveying means 74 that conveys the container as it is, and a pair of horizontal rod-shaped sealers 75 that are opposed to both outer sides of the mouth portion of the accommodation bag after accommodation,
The sealer 75 crushes the mouth of the accommodation bag P after containing the calcium oxide O5 together with the opening holding means 72 in the bag from both sides of the outside, closes the mouth, removes the opening holding means 72, and then heats it to heat the accommodation bag P. Is sealed to form a sealed bag P2. The sealed bag P2 is transported by the final conveyor C6.

(貝類の処理工程)
本実施例の処理システムによる貝類の処理方法として、下記(a)ないし(f)の工程を順に挙げることができる。先ず(a)抵抗型電気炉5の損傷を最小限に留める為に、原料貝類O1に含まれる塩分を落とす必要が有る。よって最初の工程として脱塩洗浄装置1の設置による脱塩洗浄工程が必要であり、本装置によって原料貝類O1の脱塩洗浄を行う。
(Process of shellfish processing)
As a shellfish processing method by the processing system of the present embodiment, the following steps (a) to (f) can be listed in order. First, in order to minimize damage to the resistance electric furnace 5 (a), it is necessary to drop the salt contained in the raw material shells O1. Therefore, as the first step, a desalting and cleaning step is required by installing the desalting and cleaning device 1, and the raw shellfish O1 is desalted and cleaned by this device.

(b)次に運転中の抵抗型電気炉5内での支障を未然に防ぐ手段として、様々な大きさ、形状の貝類(特に洗浄貝類O2)を出来るだけ均一に熱処理すべく、抵抗型電気炉5の炉内へ入れる際に均一な大きさ、形状にしておく必要がある、よって貝類を粗く砕く粗砕装置3にかけ、大きさを揃える粗砕行程が必要と為る。又この粗砕装置3を通すことで、脱塩洗浄工程を経た貝類の脱水工程も同時に行うことができる。   (B) Next, as a means for preventing problems in the resistance electric furnace 5 during operation, resistance type electric furnaces are used to heat-treat shells of various sizes and shapes (especially washed shellfish O2) as uniformly as possible. When putting into the furnace of the furnace 5, it is necessary to make it a uniform size and shape. Therefore, it is necessary to apply a coarse crushing process to apply the size to the crushing apparatus 3 for crushing shellfish roughly. Moreover, by passing through this crushing apparatus 3, the dehydration process of shellfish that has undergone the desalting and washing process can be performed simultaneously.

(c)次に、粗砕装置3を通って来た貝類を加熱乾燥装置4によって乾燥させ、予熱する必要がある。本炉である抵抗型電気炉5に入れる前の前処理工程として加熱乾燥装置4の予熱乾燥工程を行う。本装置によって約600℃前後の温度で乾燥処理することで熱効率が向上し、本炉(抵抗型電気炉5)での熱処理時間の短縮に繋がる。つまり加熱乾燥装置4による加熱乾燥は処理能力を上げる為の大切な行程である。この加熱乾燥装置4も電気炉とする。   (C) Next, the shells that have passed through the crushing device 3 need to be dried and preheated by the heating and drying device 4. A preheating drying process of the heating and drying apparatus 4 is performed as a pretreatment process before entering the resistance type electric furnace 5 which is a main furnace. By performing a drying process at a temperature of about 600 ° C. with this apparatus, the thermal efficiency is improved, and the heat treatment time in the main furnace (resistance type electric furnace 5) is shortened. That is, heat drying by the heat drying apparatus 4 is an important process for increasing the processing capacity. The heating and drying apparatus 4 is also an electric furnace.

(d)そして、本炉である抵抗型電気炉5において、1000℃〜1600℃の範囲内で焼成する電気焼成工程を経る。これ以上の温度になると溶融の世界に入ってしまい、この範囲以下だと焼却炉の世界となり物性を変えることが出来ない。   (D) Then, in the resistance type electric furnace 5 which is the main furnace, an electric firing process is performed in which firing is performed in a range of 1000 ° C. to 1600 ° C. If it exceeds this temperature, it will enter the world of melting, and if it is below this range, it will become the world of an incinerator and its physical properties cannot be changed.

(e)電気焼成工程によって焼成されて得た酸化カルシウムO5は高温の為、容器に溜めて貯留する貯留工程、及び容器内にて冷却器を有して常温まで冷ます冷却工程の必要がある。実施例ではこれを冷却貯留ホッパー6によって、冷却貯留工程として行っている。   (E) Calcium oxide O5 obtained by firing in the electrical firing process is hot, so it needs to be stored in a container and stored, and a cooling process in which a cooler is provided to cool the container to room temperature. . In the embodiment, this is performed as a cooling storage step by the cooling storage hopper 6.

(f)出来上がった酸化カルシウムO5は性質上吸湿性が高い事や、安全衛生法等によって規制対象となる為に速やかに樹脂製の袋に袋詰めしなければならない。この為に袋詰め装置7による袋詰め工程を必要とする。   (F) The finished calcium oxide O5 has a high hygroscopic property and must be quickly packed in a resin bag in order to be regulated by the Safety and Health Act. For this purpose, a bagging process by the bagging device 7 is required.

以上6行程を順番に具備することをもって本プラントの処理工程とする。但し、粗砕工程で脱水工程を兼ねることなく、予熱乾燥工程で脱水を行うもの、或いは運搬中に脱水工程を行うものとしても良い。他に、袋詰め工程を除いた場合でも原料貝類O1から酸化カルシウムO5を得ることができ、酸化カルシウムO5の処理方法によっては貝類の処理方法として成立する場合がある。また他に、淡水の貝類を処理する場合にも用いることができ、この場合には脱塩洗浄装置1による脱塩洗浄工程を除いて、少なくとも粗砕装置3による粗砕工程ないし抵抗型電気炉5による電気焼成工程までを順に備えた処理方法となる。   By having the above six steps in order, the processing process of this plant is taken. However, it is good also as what performs dehydration by a preheating drying process, or what performs a dehydration process during conveyance, without serving also as a dehydration process in a coarse crushing process. In addition, even when the bagging process is omitted, calcium oxide O5 can be obtained from the raw shellfish O1, and depending on the method of treating calcium oxide O5, it may be established as a shellfish processing method. In addition, it can also be used when processing freshwater shellfish. In this case, except for the desalting and washing process by the desalting and washing apparatus 1, at least a crushing process or a resistance electric furnace by the crushing apparatus 3 This is a processing method that includes the steps up to 5 for the electric firing step.

(実施例のプラントの作用)
本実施例の貝類の処理システムは、貝類を原料として連続処理可能なプラントであり、原料貝類O1を電気炉で1000℃以上の熱処理を施して処理(焼成)し、酸化カルシウムO5を得るものとなっている。また本炉として、複雑な設備が必要とならない抵抗型電気炉5によって円形経路状に移動させながら加熱処理することで、温度低下や多量の二酸化炭素の排出を伴うことなく、効率的に連続処理を行うことができ、また長時間にわたって自動運転することができる。特に脱塩洗浄装置1から抵抗型電気炉5までが組み合わされた装置群においては、貝類を対象としたことで、産業廃棄物の排出されない最終処分炉であると共に、酸化カルシウムO5を連続焼成する焼成炉となっている。
(Operation of the plant of the embodiment)
The shellfish treatment system of the present embodiment is a plant capable of continuous treatment using shellfish as a raw material, and the raw shellfish O1 is subjected to heat treatment at 1000 ° C. or higher in an electric furnace to be processed (baked) to obtain calcium oxide O5. It has become. Moreover, as a main furnace, heat treatment is carried out while moving in a circular path with a resistance electric furnace 5 that does not require complicated equipment, so that continuous processing can be efficiently performed without causing a temperature drop or a large amount of carbon dioxide emission. In addition, automatic operation can be performed for a long time. In particular, in the apparatus group in which the desalting and cleaning apparatus 1 to the resistance electric furnace 5 are combined, it is a final disposal furnace in which industrial waste is not discharged by targeting shellfish, and calcium oxide O5 is continuously fired. It is a firing furnace.

なお本処理システムは、海産の貝類のほか、海産の介類(貝のほか甲殻類、亀を含む)を処理対象物として使用することができる。また火力発電所や原子力発電所をはじめとする大型設備や海水使用施設、海洋構造物で使用することができる。   In addition, this processing system can use marine shellfish (including shellfish, shellfish and turtles) as processing objects in addition to marine shellfish. It can also be used in large facilities such as thermal power plants and nuclear power plants, seawater use facilities, and offshore structures.

このうち、特に蒸気を真水に戻すための復水器を含む設備、装置においては、多量の冷却用水を必要とし、この冷却用水として、海水を海水路によって引き込んで使用する場合がある。本処理システムはこのような設備等に組み込んで使用することが出来る。すなわちこのような設備等では、海水に含まれる貝類が海水路の壁面等に付着して、連続運転時間後には貝類が幾重にも積み重なった状態となり、やがて積み重なった下層部分からはがれ落ちる。これによって貝類が海水路の底に溜まったり機械設備の目的を損なわせたりするのを防ぐため、本考案の処理システムを組み込んだ設備にすることが好ましい。   Among these, in particular, in facilities and apparatuses including a condenser for returning steam to fresh water, a large amount of cooling water is required, and seawater may be drawn into the seawater channel for use as the cooling water. The present processing system can be used by being incorporated in such equipment. That is, in such a facility, shellfish contained in the seawater adhere to the wall surface of the seawater channel, etc., and after a continuous operation time, the shellfish are piled up several times and eventually fall off from the stacked lower layer portion. In order to prevent the shellfish from accumulating at the bottom of the seawater channel and impairing the purpose of the mechanical equipment, it is preferable to use equipment incorporating the processing system of the present invention.

また、酸化カルシウムO5を焼成する最終処分炉を含む処理システムであり、産業廃棄物は排出されない。この様に廃棄物ではなくなり産業資源の一つに成り得ることによりこれまで掛かっていた産廃費用が不要となる。従来のように廃棄物として処分するのではなく、廃棄物を工夫する事により廃棄物ではない物性に変え自然に戻すことで環境への負担を減少させるものとなっている。   Moreover, it is a processing system including a final disposal furnace for calcining calcium oxide O5, and industrial waste is not discharged. In this way, it is no longer a waste and can become one of the industrial resources, so that the industrial waste cost that has been spent so far becomes unnecessary. Instead of disposing as waste as in the past, by devising the waste, it is changed to a physical property that is not waste, and then returned to nature, thereby reducing the burden on the environment.

本処理システムによる焼成物は酸化カルシウムO5と成る。これをそのまま自然に戻すことのほか、その滅菌効果によって医療関係に使用すること、食品、飼料、ペットフードの添加剤、土壌改良肥料、凍結防止材として使用すること、強アルカリ溶液として洗剤として使用することができる。   The fired product by the present processing system is calcium oxide O5. In addition to restoring this as it is, it can be used for medical purposes due to its sterilization effect, used as an additive for food, feed, pet food, soil improvement fertilizer, anti-freezing material, and used as a detergent as a strong alkaline solution can do.

本考案の構成は以上であるが、本処理システムは上述の実施例に限定されず、本考案の趣旨を逸脱しない範囲で、構成要素の抽出、一部構成要素の削除、代替構成への置換、対象物の変更、大きさや時間、運転速度の調整といった各種変更を行うことができる。本考案はこれらの変更後の処理システムを含む。   Although the configuration of the present invention is as described above, the present processing system is not limited to the above-described embodiment, and extraction of components, deletion of some components, and replacement with alternative configurations are possible without departing from the spirit of the present invention. Various changes such as the change of the object, the size and time, and the adjustment of the driving speed can be performed. The present invention includes these modified processing systems.

1 脱塩洗浄装置
10 筒状容体
103 排水口
104 排給口
105 モーター
11 原料ホッパー
12 スクリュー羽根
121 連接板
13 噴射ノズル
2 脱塩物貯留ホッパー
21 取り込み口
22 排出バルブ
23 排出ノズル
3 粗砕装置
31 投入枠
32 ローラー
33 モーター
4 加熱乾燥装置
5 抵抗型電気炉
50 投入管
51 炉室
52 基盤
53 収集器
54 スクレーパー
6 冷却貯留ホッパー
61 本体貯留部
62 冷却器
63 回転羽根
64 排出ノズル
65 排出バルブ
7 袋詰め装置
71 引き上げ手段
72 開口保持手段
73 供給手段
74 運搬手段
75 シーラー
C 連結部
C5 連通パイプ
F ファン
O 貝類
P 収容袋
W 洗浄水
DESCRIPTION OF SYMBOLS 1 Desalination washing apparatus 10 Cylindrical container 103 Drain outlet 104 Discharge port 105 Motor 11 Raw material hopper 12 Screw blade 121 Connecting plate 13 Injection nozzle 2 Desalted substance storage hopper 21 Intake port 22 Discharge valve 23 Discharge nozzle 3 Crushing apparatus 31 Input frame 32 Roller 33 Motor 4 Heating and drying apparatus 5 Resistance type electric furnace 50 Input pipe 51 Furnace room 52 Base 53 Collector 54 Scraper 6 Cooling storage hopper 61 Main body storage part 62 Cooler 63 Rotary blade 64 Discharge nozzle 65 Discharge valve 7 Bag Stuffing device 71 Lifting means 72 Opening holding means 73 Supply means 74 Transport means 75 Sealer C Connecting portion C5 Communication pipe F Fan O Shellfish P Storage bag W Washing water

Claims (8)

海産の貝類を連続的に処理して酸化カルシウムを生産する貝類処理システムであって、
貝類を水洗することで付着塩類を除去して脱塩貝類を得る脱塩洗浄装置と、
脱塩貝類を粗砕して粗砕片を得る粗砕装置と、
粗砕片を加熱乾燥させて半焼成片を得る加熱乾燥装置と、
所定の平面経路状に伸びる炉室内に備えた移動床式の基盤上で半焼成片を焼成し、酸化カルシウムを得ると共にそれ以外の構成材を焼却する抵抗型電気炉と、
酸化カルシウムを収集して収容袋内に密封する袋詰め装置を具備してなることを特徴とする貝類処理システム。
A shell processing system that continuously processes marine shells to produce calcium oxide,
A desalting and cleaning device that removes adhering salt by washing the shellfish to obtain desalted shellfish,
A crushing device for crushing demineralized shellfish to obtain coarse fragments,
A heating and drying apparatus for drying the coarsely crushed pieces to obtain semi-baked pieces;
A resistance-type electric furnace that fires a semi-fired piece on a moving bed type base provided in a furnace chamber extending in a predetermined planar path shape, obtains calcium oxide and incinerate other constituent materials,
A shellfish processing system comprising a bagging device that collects calcium oxide and seals it in a storage bag.
抵抗型電気炉の平面視円形経路の円形内又は円形外の下方に、炉室から排出された酸化カルシウムを収集して貯留した状態で冷却する冷却ホッパーを具備し、この冷却ホッパーにて貯留した酸化カルシウムを常温にまで冷却する請求項1記載の貝類処理システム。   A cooling hopper that cools in a state in which calcium oxide discharged from the furnace chamber is collected and stored below the circular path of the resistance-type electric furnace in a circular view in plan view is stored in the cooling hopper. The shellfish processing system of Claim 1 which cools calcium oxide to normal temperature. 抵抗型電気炉が、耐熱炉材を主構成材とする耐火煉瓦からなる炉室と、多数の基盤プレートがコンベア連結された移動床式の平面視円形経路の基盤と、炉室内で基盤を動力牽引して円形経路に沿って移動させる牽引手段とを具備する請求項1または2記載の貝類処理システム。   A resistance electric furnace is a furnace room made of refractory bricks, which mainly consists of a heat-resistant furnace material, a base of a moving floor type circular path with many base plates connected to a conveyor, and the base in the furnace chamber. The shellfish processing system according to claim 1, further comprising a pulling unit that pulls and moves along a circular path. 炉室及び基盤が共に耐熱炉材を主構成材とする請求項1、2または3のいずれか記載の貝類処理システム。   The shellfish processing system according to claim 1, wherein both the furnace chamber and the base have a heat-resistant furnace material as a main constituent material. 粗砕装置は、表面に複数の突起部がそれぞれ固設された一対または複数対のローラーを各対にて並行軸状に配置してなり、各ローラーを回転駆動させながら、各対のローラー間に脱塩貝類を通すことで、所定以下の大きさに粗砕すると共に、脱塩貝類に付着した水分を落とす請求項1乃至4のいずれか記載の貝類処理システム。   The crushing device is composed of a pair or a plurality of rollers each having a plurality of protrusions fixed on the surface thereof arranged in parallel shafts in each pair, and while rotating each roller, between each pair of rollers The shellfish treatment system according to any one of claims 1 to 4, wherein the shellfish processing system according to any one of claims 1 to 4, wherein the shellfish is crushed to a predetermined size or less by passing the desalted shellfish through, and water attached to the desalt shellfish is removed. 袋詰め装置は、収容袋の口部を一枚ずつ引き上げて、口部内で水平の環状に広がることで、収容袋を開口した状態で吊下げ保持する帯板状の開口保持手段と、開口保持手段で開口した収容袋内に酸化カルシウムを供給する供給手段と、収容後の収容袋の口部の両外側に対向して一対設けられた水平棒状体のシーラーとを具備してなり、
シーラーは、酸化カルシウム収容後の収容袋の口部を外側の対向両面から押しつぶして収容袋を閉口させ、開口保持手段を抜き取ったのちに加熱して収容袋を密閉するものである請求項1乃至5のいずれか記載の貝類処理システム。
The bagging device includes a band plate-shaped opening holding means for holding and holding the storage bag in an opened state by pulling up the mouth of the storage bag one by one and spreading it horizontally in the mouth, and holding the opening A supply means for supplying calcium oxide into the accommodation bag opened by the means, and a pair of horizontal bar sealers provided opposite to both outer sides of the mouth portion of the accommodation bag after accommodation,
The sealer crushes the mouth portion of the accommodation bag after containing calcium oxide from both opposite sides of the outer side to close the accommodation bag, and after removing the opening holding means, heats up and seals the accommodation bag. The shellfish treatment system according to any one of 5.
脱塩洗浄装置は、上部の拡径した投入口から海水つきの貝類を収容し、下部の縮径した排出口から排出する縦型筒状の貯留ホッパーと、貯留ホッパーの下方にて下連通部に上部連通し、この下連通部から斜め上方へ伸長する筒状容体と、筒状容体の伸長方向に沿って軸設され、軸周りにらせん状に連続形成された回転可能なスクリュー羽根と、筒状容体内の下連通部よりも上方の天井部に配置されて内部に洗浄水を噴射する複数の噴射ノズルとを備えてなり、
筒状容体は、下連通部よりも下方の底部に設けられ、筒状容体内の水を排出する排水口と、筒状容体内の上方伸長先の底部に設けられ、容体内の貝類を外部へ排給する排給口を備え、
排水口からの排水量の自動調整によって、噴射ノズルから噴射された洗浄水量を所定範囲内に保つことで容体内に洗浄水を一定水位で保持するものであり、
貯留ホッパーから供給された海水付きの貝類を筒状容体内の洗浄水内に浸漬させて伸長方向上方へ回転させながら運搬し、この運搬した浸漬後の貝類を、洗浄水の水面上方にて噴射ノズルによって洗浄したのちに、排給口から外部へ排給することで貝類を脱塩する請求項1乃至6のいずれか記載の貝類処理システム。
The desalting and cleaning device is a vertical cylindrical storage hopper that accommodates shellfish with seawater from the upper diameter of the inlet and discharges from the lower diameter outlet, and the lower communication part below the storage hopper. A cylindrical container extending obliquely upward from the lower communication part, a rotatable screw blade axially provided along the extending direction of the cylindrical container, and continuously formed in a spiral around the axis; A plurality of injection nozzles arranged on the ceiling portion above the lower communication portion of the container to inject cleaning water into the interior;
The cylindrical container is provided at the bottom below the lower communication part, and is provided at a drain outlet for discharging water in the cylindrical container, and at the bottom of the upper extension destination in the cylindrical container. Equipped with a discharge port for discharging to
By automatically adjusting the amount of water discharged from the drain port, the amount of cleaning water sprayed from the spray nozzle is kept within a predetermined range, thereby holding the cleaning water at a constant level in the container.
The shellfish with seawater supplied from the storage hopper is immersed in the cleaning water in the cylindrical container and transported while rotating upward in the extension direction, and the transported shellfish after injection is sprayed above the surface of the cleaning water. The shellfish processing system according to any one of claims 1 to 6, wherein the shellfish is desalted by being discharged from a discharge port to the outside after being washed by a nozzle.
スクリュー羽根には、回転軸方向に隣り合う羽根板間をつなぐ連接板が、回転軸周りに等間隔に複数枚固設されてなり、各連接板は、回転軸方向に対して軸側面視及び軸断面視の両方で傾斜して配置された請求項7記載の貝類処理システム。
A plurality of connecting plates connecting blade plates adjacent to each other in the rotational axis direction are fixed to the screw blades at equal intervals around the rotational axis, and each connecting plate has an axial side view and a rotational axis direction. The shellfish processing system according to claim 7, wherein the shell processing system is disposed so as to be inclined in both axial sectional views.
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010163351A (en) * 2009-02-02 2010-07-29 Hideo Yano Shellfish treatment system and treatment method for shellfish
JP2011147854A (en) * 2010-01-19 2011-08-04 Yanagida Sangyo Kk Method and system for treating marine shellfish

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010163351A (en) * 2009-02-02 2010-07-29 Hideo Yano Shellfish treatment system and treatment method for shellfish
JP2012025651A (en) * 2009-02-02 2012-02-09 Hideo Yano Shellfish treatment system and treatment method for shellfish
JP2011147854A (en) * 2010-01-19 2011-08-04 Yanagida Sangyo Kk Method and system for treating marine shellfish

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