JPS6384628A - Storage apparatus - Google Patents

Storage apparatus

Info

Publication number
JPS6384628A
JPS6384628A JP61228421A JP22842186A JPS6384628A JP S6384628 A JPS6384628 A JP S6384628A JP 61228421 A JP61228421 A JP 61228421A JP 22842186 A JP22842186 A JP 22842186A JP S6384628 A JPS6384628 A JP S6384628A
Authority
JP
Japan
Prior art keywords
granular molded
molded product
granular
storage
storage tank
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.)
Granted
Application number
JP61228421A
Other languages
Japanese (ja)
Other versions
JPH0543413B2 (en
Inventor
Michio Kitagawa
道夫 北川
Yoshiki Kuroda
黒田 芳喜
Toshimitsu Aoki
青木 敏光
Tsutomu Higo
勉 肥後
Shigeru Yamaguchi
繁 山口
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.)
Ebara Corp
Original Assignee
Ebara Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ebara Corp filed Critical Ebara Corp
Priority to JP61228421A priority Critical patent/JPS6384628A/en
Publication of JPS6384628A publication Critical patent/JPS6384628A/en
Publication of JPH0543413B2 publication Critical patent/JPH0543413B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0015Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
    • B01J8/0035Periodical feeding or evacuation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)
  • Glanulating (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Abstract

PURPOSE:To prevent the compact conglomeration of granular molded articles by once holding the granular molded articles which are obtained by humidifying and molding fine particles contg. substance forming hydrated salt in a receptacle and thereafter rotating the receptacle and allowing the granular molded articles held on the receptacle to fall into a storage part. CONSTITUTION:Granular molded articles which are obtained by humidifying and molding fine particles contg. substance forming hydrated salt such as cement are fed into a receptacle 1 through a feed port 3 and once held on a pan 6. After fixed time elapses and solidification is advanced with some degrees, the pan 6 is rotated and slanted at about 50-70 deg.C i.e. to the left with a horizontal rotary shaft 5. At this time, the pan 6 is preferably positioned so that it is made to an introduction chute for a storage tank 7. The granular molded articles held on the pan 6 are slid and introduced into the left storage tank 7 through an introduction port 8 via a left discharge port 4. Thereby compact conglomeration and the generation of a bridge in the storage tank 7 can be prevented by once receiving the granular molded articles in the receptacle 1 and aging them to some degree.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、微細粒子を主体とする物質を、水和塩成長反
応を用いて粒状固体に成形固化して排出するに際し、水
和塩形成物質を含む微細粒子を加湿成形した粒状成形品
を貯留することにより、水和塩成長反応を行わしめて当
該粒状成形品を粒状固化へと変成せしめ、該粒状固体を
排出する貯留装置の改善に関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention is directed to the formation of hydrated salts when a substance mainly consisting of fine particles is solidified into granular solids and discharged using a hydrated salt growth reaction. Related to improvement of a storage device that stores a granular molded product obtained by humidifying and molding fine particles containing a substance, performs a hydrated salt growth reaction, transforms the granular molded product into solidified granules, and discharges the granular solid. It is.

特には、貯留装置内において、セメント、カルシウム塩
、マグネシウム塩等の水和塩成長反応を利用して、乾燥
した又は低含水の微細粒子を主体とする物質を粒状に成
形し固化処理する際の養生を行わしめる様にしたもので
あって、対象物質である微細粒子としては、例えば都市
ごみ、下水汚泥等の廃棄物、石炭、パーク、バガス、廃
木材等の固体燃料等の灰、各種排ガス処理や排水処理プ
ロセスで排出されるスラッジやダストなどをあげること
ができる。
In particular, in a storage device, a substance consisting mainly of dry or low water content fine particles is shaped into granules and solidified using the growth reaction of hydrated salts such as cement, calcium salts, magnesium salts, etc. The fine particles that are targeted include, for example, municipal waste, waste such as sewage sludge, ash of solid fuels such as coal, park, bagasse, and waste wood, and various exhaust gases. Examples include sludge and dust discharged during wastewater treatment and wastewater treatment processes.

〔従来の技術及び発明が解決しようとする問題点〕上述
した様な灰、スラッジ、ダスト等は、そのままでは運搬
のための車両積載時や最終処分地での荷おろし時に激し
い粉じんを発生したり、流出あるいは付着したり、最終
処分地でも風により舞い上がったりしてしまう。また、
重金属や有機塩素化合物などの有害物質を含んでいるも
のでは、環境汚染の心配もある。
[Problems to be solved by the conventional technology and invention] Ash, sludge, dust, etc. as mentioned above, if left as is, generate heavy dust when loaded onto a vehicle for transportation or unloaded at a final disposal site. , they may flow out or stick to each other, or they may be blown up by the wind at the final disposal site. Also,
There are also concerns about environmental pollution if they contain hazardous substances such as heavy metals and organic chlorine compounds.

そこで、最近では、それらの問題解決の手段として、必
要ならばセメントその他の水和塩形成物質(以下単に「
セメント」と称する)と混合の上粒状成形した後に排出
することが採用されはじめている。
Therefore, recently, as a means to solve these problems, cement and other hydrated salt-forming substances (hereinafter simply "
It is beginning to be adopted to mix it with cement (referred to as "cement"), form it into granules, and then discharge it.

即ち、対象となる微細粒子を主体とする物質に、セメン
トを添加するが、あらかじめその成分としてカルシウム
塩やマグネシウム塩を含有しており水添加により水和塩
成長反応を起こして固化するものであれば、特にセメン
トは添加せずに、加湿や混練、成形工程を経て硬めの泥
状物の粒状成形品とし、それを養生して水和塩成長反応
を行わせ、運搬に伴う扱いにある程度耐え、最終処分地
で雨風にさらされても所望の耐久性をあられす程度に、
固化反応を進めた上で搬出している。この加湿は、微細
粒子の径や種類、粒状成形手段、水溶塩含有量等により
巾があるが、通常は重量で8〜30%程度、付着や発し
んを抑えようとすれば12〜20%程度の水分量とする
ことが良く、また実験的にも確認されている。
In other words, cement is added to the target substance, which consists mainly of fine particles, but it may contain calcium salts or magnesium salts as a component in advance, and solidify by causing a hydrated salt growth reaction when water is added. For example, without adding any cement, a hard slurry is formed into a granular product through humidification, kneading, and molding processes, and then it is cured to undergo a hydrated salt growth reaction, so that it can withstand the handling involved in transportation to some extent. , to the extent that it maintains the desired durability even when exposed to the elements at the final disposal site.
It is transported out after the solidification reaction has progressed. This humidification varies depending on the diameter and type of fine particles, the granulation method, the water-soluble salt content, etc., but it is usually about 8 to 30% by weight, and about 12 to 20% if you want to suppress adhesion and eruption. It is recommended to keep the water content at 100%, and this has also been confirmed experimentally.

ところで、単に養生すると言っても、成形工程直後にお
いては硬めの泥状物の粒状成形品であって、粒同士湿潤
状態でかつ軟らかいために互いに付着してしまう。この
粒状成形品を単に貯留部に投入貯留するのでは、十分固
化しないうちに貯留部に投入されることになり、貯留部
内で折角の粒状成形品が互いに付着しあい圧密化、団塊
化してしまうことが起こる。特に転造粒状成形では、原
理的に粒状成形品の表面に水がしみ出した形となるため
、この傾向が強い。これは、加湿水量が多めで起こり易
いが、かといって少なめとすると発じんし易くなり問題
となってしまう。
By the way, even though it is simply curing, it is a granular molded product of hard muddy material immediately after the molding process, and since the grains are wet and soft, they stick to each other. If this granular molded product is simply charged and stored in the storage section, it will be thrown into the storage section before it has solidified sufficiently, and the granular molded products will adhere to each other in the storage section and become compacted and aggregated. happens. This tendency is particularly strong in rolling granulation molding, because in principle water seeps onto the surface of the granular molded product. This is likely to occur if the amount of humidifying water is too large, but if it is too small, dust is likely to be generated, which becomes a problem.

粒状成形品が互いに付着し団塊化すると、貯留部の底全
面が排出ゲートの様なバンカ構造であっても、下面ゲー
トを開いても排出できないいわゆるブリッジ状態になり
、場合によっては全体が一つに団塊化する。また、なん
とか排出しても、大きな数百kgから1トンを超える塊
で車両荷台に落下することになり、その衝撃が車両をい
ため、片積みとなると運搬走行中のバランスがとれない
とか、最終処分地での扱いに困る。
When the granular molded products adhere to each other and form agglomerates, even if the entire bottom of the storage part has a bunker structure like a discharge gate, it becomes a so-called bridge state that cannot be discharged even if the bottom gate is opened, and in some cases, the entire bottom becomes one. will become a baby boom. Also, even if they are somehow ejected, large chunks weighing from several hundred kg to more than one ton will fall onto the vehicle loading platform, and the impact will damage the vehicle. Difficult to handle at disposal site.

従って、そのために、従来様々の手段がとられている。Therefore, various measures have been conventionally taken for this purpose.

その中に、−旦装置きしある程度固化反応を進め、その
上で貯留部に投入すると、投入の際にその落下の衝撃等
により、それまでの粒同士の付着が未だ十分固化してい
ないために、崩れたり離れたりして壊れ、再度バラ積み
の状態となり、しかも既に固化がある程度進んでいるた
めに、それほど付着、団塊化が起きないという方式があ
る。
Once the solidification reaction has proceeded to some extent through the device, the solidification reaction may proceed to a certain extent, and then the particles are poured into the storage section.The adhesion of the particles to each other may not yet solidify due to the impact of the particles falling during the feeding. Another method is that the materials crumble or separate, break, and become piled up again, and since they have already solidified to some extent, they do not adhere to each other or form clumps as much.

例えば、養生コンベヤと称して、ゆっくりとないしは間
欠的に寸動する巾広コンベヤベルト上に粒状成形品を積
載し、そのベルト上での滞留時間で固化時間を稼ぐ方式
がある。
For example, there is a method called a curing conveyor in which granular molded products are loaded on a wide conveyor belt that moves slowly or intermittently, and the solidification time is gained by the residence time on the belt.

しかしながらこの方式では、大きなコンベヤでしかも特
殊な動きをさせるため、コストがががり大きな空間をも
必要とした。また、ベルトへの固化粒子の付着を避けら
れず、傷みは激しく、リターンローラやベルト反転部等
での汚れ、付着等もひどく、メンテナンスが大変で、作
業環境もどうしても粉じんだらけとなり、好ましいもの
ではなかった。
However, this method requires a large conveyor and special movements, which increases costs and requires a large space. In addition, the adhesion of solidified particles to the belt cannot be avoided, causing severe damage, dirt and adhesion on return rollers, belt reversing parts, etc., making maintenance difficult and the work environment inevitably full of dust, which is not desirable. There wasn't.

また、第3図に示す様に、貯留槽21の上に下面に開閉
ゲート23を持つサブホッパ22を連接し、このサブホ
ッパ22に一旦粒状成形品を受け入れ、一定時間毎にゲ
ート回転軸24を回転させて開閉ゲート23を左右交互
に開いて粒状成形品を貯留槽21に落し込み、固化した
粒状固体を排出ゲート回転輪250回転により排出ゲー
ト26を開いて排出させるものもあった。
In addition, as shown in FIG. 3, a sub-hopper 22 having an opening/closing gate 23 on the lower surface is connected above the storage tank 21, and the sub-hopper 22 once receives the granular molded product, and the gate rotating shaft 24 is rotated at regular intervals. In some cases, the granular molded product is dropped into the storage tank 21 by opening the opening and closing gates 23 alternately on the left and right sides, and the solidified granular solid is discharged by opening the discharge gate 26 by rotating the discharge gate rotating wheel 250 times.

それによれば、確かに大きなベルトコンベヤは不要とな
るが、ゲート回転軸24の駆動用のシリンダを必要とし
、またサブホッパ22の分貯留槽21がかさ上げされる
にもかかわらず、貯留槽21の断面積を増やすことはで
きず、大きな貯留容量を得にくかった。従って、貯留容
量を大きくするためには、それぞれサブホッパを備えた
貯留槽を複数並設し、各サブホッパを切替コンベヤで結
んでやらねばならず、この切替コンベヤについても前述
の養生コンベヤと同様の問題があった。
According to this, a large belt conveyor is certainly unnecessary, but a cylinder for driving the gate rotation shaft 24 is required, and even though the storage tank 21 of the sub-hopper 22 is raised, the storage tank 21 It was not possible to increase the cross-sectional area, making it difficult to obtain a large storage capacity. Therefore, in order to increase the storage capacity, it is necessary to install multiple storage tanks, each with a sub-hopper, and connect each sub-hopper with a switching conveyor, and this switching conveyor also has the same problem as the curing conveyor described above. was there.

本発明は、このような種々の問題点を解決し、粒状成形
品の貯留固化に際し、団塊化することを防ぎ、貯留部内
でブリッジを生ずるおそれがなく、円滑な排出を可能に
し、貯留槽を用いた貯留部形式にあっても貯留容量の大
容量化による貯留槽の複数化にも容易に対応可能ならし
める貯留装置を提供することを目的とするものである。
The present invention solves these various problems, prevents agglomeration when storing and solidifying granular molded products, eliminates the risk of bridging in the storage part, enables smooth discharge, and improves the storage tank. It is an object of the present invention to provide a storage device that can easily accommodate a plurality of storage tanks due to an increase in storage capacity, regardless of the type of storage section used.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は、微細粒子を水和塩成長反応を用いて粒状固体
に成形固化して排出するための貯留装置であって、水和
塩形成物質を含む微細粒子を加湿成形した粒状成形品の
供給口を上部に有し、下部に排出口を有し、さらに内部
に前記供給口に供給される粒状成形品を受けかつ水平回
転軸により回転可能たらしめた受け皿を備えた受け容器
と、上部に投入口を有し、かつ排出機構を備えた貯留部
とからなり、前記受け容器をその排出口が前記貯留部の
投入口に連通可能に配設し、前記受け皿の回転により受
け皿上の粒状成形品が前記貯留部内に落下する如く構成
したことを特徴とする貯留装置を提供するものである。
The present invention is a storage device for molding and solidifying fine particles into granular solids using a hydrated salt growth reaction and discharging them, and supplies granular molded products obtained by humidifying and molding fine particles containing hydrated salt-forming substances. A receiving container having a mouth at an upper part, a discharge port at a lower part, and a receiving tray inside which receives a granular molded product supplied to the supply port and is rotatable by a horizontal rotation axis; a storage part having an input port and a discharge mechanism, the receiving container is disposed so that its discharge port can communicate with the input port of the storage part, and the granular molding on the receiving tray is performed by rotating the receiving tray. The present invention provides a storage device characterized in that the product is configured to fall into the storage section.

〔作 用〕[For production]

上記の様な本発明の構成により、セメントを含む微細粒
子を加湿成形した粒状成形品は、供給口から受け容器内
に供給され、内部の受け皿上に一定時間受けとめられた
のち、水平回転軸の回転によって受け皿は回転、傾斜し
、粒状成形品は排出口から投入口を経て貯留部内に滑り
落ちる。この様に受け皿は粒状成形品を一定時間保持し
ては回転して貯留部内に落下させることを繰り返し、こ
の保持時間のうちに特に当初に受け容器に供給されたも
のはある程度の固化が進む。
With the configuration of the present invention as described above, the granular molded product obtained by humidifying and molding fine particles containing cement is supplied into the receiving container from the supply port, and after being received on the internal receiving tray for a certain period of time, it is placed on the horizontal rotating shaft. As a result of the rotation, the tray rotates and tilts, and the granular molded product slides from the discharge port through the input port into the storage section. In this manner, the receiving tray repeatedly holds the granular molded product for a certain period of time, rotates, and drops it into the storage section, and during this holding time, the particulate product initially supplied to the receiving container progresses to a certain degree of solidification.

粒状成形品は受け皿に一定時間保持されているうちに固
化が進むことにより、変形も少なく付着性もかなり失わ
れており、たとえ互いに付着していても受け皿回転によ
り貯留部に落下した時の衝撃によってばらされ、保持時
間の終わりに近く受け容器に供給されたものを除けば貯
留部において圧密化や団塊化はあまり生じなくなる。そ
して、搬出等のための排出の際には、容易にばらばらと
なり、排出及び搬送や最終処分地での扱いも容易になり
、かつ粉じん発生や有害物質の拡散も抑制することがで
きることになる。
As the granular molded products solidify while being held in the tray for a certain period of time, they undergo little deformation and lose a considerable amount of adhesion. There is little compaction or agglomeration in the reservoir, except for that which is broken up by the material and fed into the receiving vessel near the end of the holding period. Then, when it is discharged for transport, etc., it is easily broken up into pieces, making it easier to discharge, transport, and handle at the final disposal site, and also to suppress the generation of dust and the spread of harmful substances.

〔実施例〕〔Example〕

本発明の一実施例を第1図を参照しながら説明すれば、
1は受け容器であって、セメントを含む微細粒子を加湿
成形した粒状成形品2が供給される供給口3が上部に設
けられ、下部には排出口4が設けられている。さらに、
受け容器1内には供給口3から供給される粒状成形品2
を受けかつ水平回転軸5に固定された受け皿6が備えら
れ、水平回転軸5には、図示しない回転駆動装置とその
回転の制御系統からなる回転機構が付属されている。
An embodiment of the present invention will be described with reference to FIG.
Reference numeral 1 denotes a receiving container, which is provided with a supply port 3 at the top thereof, through which a granular molded product 2 obtained by humidifying and molding fine particles containing cement is provided, and a discharge port 4 is provided at the bottom. moreover,
Inside the receiving container 1, a granular molded product 2 is supplied from the supply port 3.
A receiving tray 6 is provided which receives the horizontal rotating shaft 5 and is fixed to the horizontal rotating shaft 5, and the horizontal rotating shaft 5 is attached with a rotating mechanism consisting of a rotational drive device (not shown) and a control system for its rotation.

7は貯留槽であって、貯留槽7の上部には投入口8が開
口し、下部には排出ゲート回転軸9により回転開閉され
る排出ゲート10が設けられている。
Reference numeral 7 denotes a storage tank, and an input port 8 is opened in the upper part of the storage tank 7, and a discharge gate 10 that is rotated to be opened and closed by a discharge gate rotating shaft 9 is provided in the lower part.

さらに、受け容器1を貯留槽7の上方に設置し、受け容
器1の排出口4が貯留槽7の投入口8に連通できるよう
にし、受け皿6の回転によって受け皿6上の粒状成形品
が貯留槽7内に落下する如くなっている。これは、例え
ば第1図示例の様に、受け皿6が回転して傾斜した時に
、受け皿6が粒状成形品の貯留槽7への投入シュートと
なる様に位置決めしておくことが好ましく、受け皿6自
体を傾斜シュートとして利用することで、受け容器1と
供給口3への供給機構(図示せず)との接続位置と貯留
槽7への投入位置を離れたものとし、かつコンベヤ等を
用いることなしに投入位置相互についても互いに離れた
ものとすることも容易となる。
Further, the receiving container 1 is installed above the storage tank 7 so that the outlet 4 of the receiving container 1 can communicate with the input port 8 of the storage tank 7, and the granular molded products on the receiving tray 6 are stored by rotating the receiving container 6. It is designed to fall into the tank 7. For example, as shown in the first illustrated example, when the tray 6 rotates and tilts, it is preferable to position the tray 6 so that it becomes a chute for introducing the granular molded product into the storage tank 7. By using itself as an inclined chute, the connection position between the receiving container 1 and the supply mechanism (not shown) to the supply port 3 and the charging position into the storage tank 7 can be separated, and a conveyor or the like can be used. It is also easy to set the input positions apart from each other.

従って、貯留槽7は1個でもよいが、図示例の様に2ケ
所の排出口4に対しそれぞれ1個の計2個並設し、受け
容器1下部の排出口4を両側に設けて各排出口4を各貯
留槽7の投入口8に連通させ、受け皿6を水平回転軸5
対して交互に反対側に回転、傾斜させることで、各貯留
槽7に分配することが可能になり、さらに受け容器1を
そのほぼ中心を通る垂直軸11を中心に906あるいは
60”ずつ回転させることで、4個又は6個の貯留槽へ
分配することも容易に可能となる。
Therefore, the number of storage tanks 7 may be one, but as shown in the example shown, two storage tanks 7 are installed in parallel, one for each of the two discharge ports 4, and the discharge ports 4 at the bottom of the receiving container 1 are provided on both sides. The discharge port 4 is connected to the input port 8 of each storage tank 7, and the tray 6 is connected to the horizontal rotation shaft 5.
By alternately rotating and tilting the receiving container 1 to the opposite side, it becomes possible to distribute the distribution to each storage tank 7, and further, the receiving container 1 is rotated by 906 or 60" around the vertical axis 11 passing approximately through its center. This makes it easy to distribute to 4 or 6 storage tanks.

なお、受け容器1の供給口3へ粒状成形品2を供給する
ための供給機構は図示していないが、特に粒状成形のた
めの装置が離れた距離にあればベルトコンベヤ等の搬送
機器を必要とするが、受け容器1の直上に粒状成形のた
めの装置の粒状成形品出口があれば接続シュートを付設
するのみでよい。
Note that although a feeding mechanism for feeding the granular molded product 2 to the supply port 3 of the receiving container 1 is not shown, a conveying device such as a belt conveyor is required especially if the granular molding device is located at a distance. However, if the granule molded product outlet of the granule molding device is located directly above the receiving container 1, it is only necessary to attach a connecting chute.

しかして、セメントを含む微細粒子を加湿成形した粒状
成形品2は、供給口3から受け容器1内に供給されて受
け皿6上に一旦保持される。そして一定時間経過後、受
け容器1が満杯になる前に、例えば左側貯留槽7であれ
ば左側に50〜70″程度水平回転軸5によって受け皿
6を回転し、傾斜させ、受け皿6上の粒状成形品を重力
によって滑落させ、左側排出口4を経て投入口8から左
側貯留槽7に投入する。これは右側についても同様であ
る。
Thus, the granular molded product 2 obtained by humidifying and molding fine particles containing cement is supplied into the receiving container 1 from the supply port 3 and is temporarily held on the receiving tray 6. Then, after a certain period of time has elapsed, before the receiving container 1 is full, for example, in the case of the left storage tank 7, the receiving tray 6 is rotated and tilted by the horizontal rotating shaft 5 by about 50 to 70'' to the left, so that the particles on the receiving tray 6 are The molded product is allowed to slide down by gravity and is fed into the left side storage tank 7 through the left side discharge port 4 and the input port 8. The same applies to the right side.

受け皿60回転角度は、受け皿6上の粒状成形品が重力
によって滑落する角度以上にする必要があるが、受け皿
6に付着するなどしてなかなか落ちにくいことも生じる
ので、受け皿6の粒状成形品を載せる面には、例えばテ
フロン、ポリエチレン、その他の剥離性の良い材質のも
のを塗布したり張ったりして、剥離し易くする事が必要
である。
The rotation angle of the tray 6 must be greater than the angle at which the granular molded product on the tray 6 slides down due to gravity, but since it may stick to the tray 6 and be difficult to fall off, The surface on which it is placed needs to be coated or covered with, for example, Teflon, polyethylene, or other material with good releasability to make it easier to peel off.

特に付着し易い場合には、受け容器1内で粒状成形品が
触れる部分全てに同様の処理をすることが望ましい。場
合によっては、それらの部分を軟質プラスチックやゴム
などの変形し易い材料等で変形し易くしておくと、受け
皿6を傾斜させる際の荷重の移動などで受け皿6等を変
形して剥離させることができ、粒状成形品が受け容器l
に供給された時にはやわらかく湿潤状態にあるために付
着していても、受け皿6を傾斜させ、受け容器lから排
出される時にはある程度固化ないし乾燥化しており、受
け皿6等の変形で剥離し易くなっているために効果があ
る。
If the particles are particularly prone to adhesion, it is desirable to apply the same treatment to all parts of the receiving container 1 that come into contact with the granular molded product. In some cases, if these parts are made of easily deformable materials such as soft plastic or rubber, the tray 6 etc. may be deformed and peeled off due to the movement of the load when tilting the tray 6. is completed, and the granular molded product is placed in a receiving container.
Even if it adheres because it is in a soft and wet state when it is supplied to the container, it will be solidified or dried to some extent by the time the tray 6 is tilted and the container 1 is discharged, and it will easily peel off due to the deformation of the tray 6, etc. It is effective because it is

なお、受け容器1の容量は、下方の貯留槽7で圧密化、
団塊化しないよう、少なくとも粒状成形品を排出した直
後に受け入れた次の粒状成形品が、付着性と変形性を失
う程度以上の滞留時間に見合ったものとすることが必要
で、水和塩成長反応速度と粒状成形品の成形処理速度に
よって決まる。
The capacity of the receiving container 1 is determined by compaction in the storage tank 7 below.
In order to avoid agglomeration, it is necessary that the next granular molded product received immediately after the granular molded product is discharged must have a residence time that is at least long enough to lose its adhesion and deformability, and prevent hydrated salt growth. It is determined by the reaction rate and the molding processing speed of the granular molded product.

例えば、アルミナセメント等の早強特殊セメントを使う
と10分前後の短時間で十分であるが、−般ボルトラン
ドセメント並の反応速度であれば、少なくとも20分か
ら1時間以上の滞留時間が望ましい。反応速度や乾燥化
を促進するために、受け容器1内に熱風を供給したり、
換気を行ったりするのも、容積を小さくしたり圧密団塊
防止効果の増強に望ましい。
For example, if a special early-strengthening cement such as alumina cement is used, a short time of around 10 minutes is sufficient, but if the reaction rate is comparable to general Bortland cement, a residence time of at least 20 minutes to 1 hour or more is desirable. In order to accelerate the reaction rate and drying, hot air is supplied into the receiving container 1,
Ventilation is also desirable to reduce the volume and enhance the effect of preventing compaction.

このようにして、ある程度固化ないし乾燥化した粒状成
形品は、貯留槽7で更に水和塩成長反応、あるいは乾燥
等による固化を進めて養生し、かつ搬出に備えての貯留
を行った後、排出ゲート回転軸9により排出ゲート10
を開き、車両等に積載し、搬出する。
In this way, the granular molded product that has been solidified or dried to some extent is cured in the storage tank 7 by further solidifying through hydrate salt growth reaction or drying, and then stored in preparation for transport. The discharge gate 10 is rotated by the discharge gate rotation shaft 9.
Open it, load it onto a vehicle, etc., and transport it.

また、必要であれば、垂直軸11を中心にほぼ等距離に
貯留槽7を4個又は6個並設し、受け容器1を垂直軸1
1を中心にほぼ90°又は60″回転し、各貯留槽7へ
粒状成形品を分配することも容易に可能となる。
If necessary, four or six storage tanks 7 may be arranged in parallel at approximately equal distances around the vertical axis 11, and the receiving container 1 may be placed in parallel with the vertical axis 11.
It is also possible to easily distribute the granular molded product to each storage tank 7 by rotating approximately 90° or 60″ around the center.

第2図は本発明の他の実施例を示し、第1図示例では受
け皿6の回転は粒状成形品滑落後瞬時に復帰させなくて
はならないが、第2図示例では受け皿6を水平回転軸5
を中心に3等分して配置したもので、120°又は24
0@ずつ間欠的な回転を左右に行わせることにより貯留
槽7への投入と同時に受け皿6の切り換えを行うもので
ある。
FIG. 2 shows another embodiment of the present invention. In the first illustrated example, the rotation of the tray 6 must be returned instantaneously after the granular molded product slides down, but in the second illustrated example, the rotation of the tray 6 is rotated around a horizontal rotation axis. 5
It is divided into three equal parts around the center, and the angle is 120° or 24
By intermittent rotation left and right by 0@, the tray 6 is switched at the same time as it is poured into the storage tank 7.

この場合、受け容器1の下部を左右の貯留槽7をつなぐ
つなぎ板12としである。もち論、受け皿6を平板とし
て180@ずつ回転させるようにしても良く、この場合
、駆動はエアシリンダなどとし、シリンダが伸びる際に
一方の貯留槽7に投入し、伸びた状態で粒状成形品を受
け入れ、一定時間後こんどはシリンダが縮む際に他方の
貯留槽7に投入し、縮んだ状態で粒状成形品を受け入れ
、一定時間後再びシリンダを伸ばす、という形で運転す
ることができ、駆動制御が簡単となる利点がある。
In this case, the lower part of the receiving container 1 is used as a connecting plate 12 that connects the left and right storage tanks 7. Of course, the tray 6 may be a flat plate and rotated by 180@. In this case, the driving force is an air cylinder, etc., and when the cylinder is stretched, it is put into one of the storage tanks 7, and the granular molded product is stored in the stretched state. After a certain period of time, when the cylinder contracts, it is put into the other storage tank 7, the granular molded product is received in the contracted state, and after a certain period of time, the cylinder is extended again. This has the advantage of being easy to control.

本実施例も第1図示例とほとんど同様の作用を示すが、
受け皿6の傾斜角は垂直又はそれ以上となり、粒状成形
品が受け皿6へ残留する不安がない。なお、受け皿6か
ら直接貯留槽7に落下せず、つなぎ板12上に落ちたも
のも、回転する受け皿6の先端で貯留槽7に掃き落とさ
れるため問題はない。
This example also exhibits almost the same effect as the first illustrated example, but
The angle of inclination of the tray 6 is vertical or more, so there is no fear that the granular molded product will remain on the tray 6. Incidentally, there is no problem even if the objects do not fall directly from the receiving tray 6 into the storage tank 7 but fall onto the connecting plate 12 because they are swept into the storage tank 7 by the tip of the rotating receiving tray 6.

以上の実施例のいずれについても言えることであるが、
貯留槽7としては例示された形式のものに限定されるも
のではなく、土間貯留としてシャベルローダ等ですくい
あげる形で排出するものや、ピット貯留としてパケット
付走行うレーンにより搬出用の車両に積載するようなも
のであってももちろん良い。そのようなものであっても
投入位置を分散させることにより、貯留される粒状成形
品の山を複数形成させて貯留空間を有効利用することに
なることは言うまでもない。
As can be said for any of the above examples,
The storage tank 7 is not limited to the type shown, but may be one that is stored on an earthen floor and is scooped up and discharged with a shovel loader, or one that is stored in a pit that is loaded onto a vehicle for transport using a lane that runs with packets. Of course it's fine if it's something you do. It goes without saying that even in such a case, by distributing the feeding positions, a plurality of piles of stored granular molded products can be formed and the storage space can be effectively utilized.

〔発明の効果〕〔Effect of the invention〕

以上述べた様に本発明によれば、セメントを含む微細粒
子を加湿成形した粒状成形品を、−旦受け容器に受けて
固化をある程度おこなわせ、付着性や変形性を減殺した
のち貯留部に落下させることで、貯留部における粒状成
形品の圧密団塊化やブリッジ発生を防止し、防じん、扱
い性の向上、有害物質対策等を有効ならしめる効果が生
じ、さらに−軸による受け皿の回転を採用したことによ
す構造は単純でコンパクトになり、かつ複数の貯留部へ
の分配も容易になる等、本発明の微細粒子の粒状固化処
理に対する貢献は大である。
As described above, according to the present invention, a granular molded product obtained by humidifying and molding fine particles containing cement is first received in a receiving container and solidified to some extent to reduce adhesiveness and deformability, and then placed in a storage part. Dropping prevents compaction and bridging of granular molded products in the storage area, and effectively prevents dust, improves handling, and prevents harmful substances.Furthermore, the tray is rotated by a shaft. As a result, the structure of the present invention is simple and compact, and distribution to a plurality of reservoirs is facilitated, making the present invention a significant contribution to the granular solidification process of fine particles.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図及び第2図はそれぞれ本発明の実施例を示す断面
図で、第3図は従来例を示す断面図である。 1・・・受け容器、2・・・粒状成形品、3・・・供給
口、4・・・排出口、5・・・水平回転軸、6・・・受
け皿、7・・・貯留槽、8・・・投入口、9・・・排出
ゲート回転軸、10・・・排出ゲート、11・・・垂直
軸、12・・・つなぎ板、21・・・貯留槽、22・・
・サブホッパ、23・・・開閉ゲート、24・・・ゲー
ト回転軸、25・・・排出ゲート回転軸、26・・・排
出ゲート。
1 and 2 are sectional views showing an embodiment of the present invention, and FIG. 3 is a sectional view showing a conventional example. DESCRIPTION OF SYMBOLS 1... Receiving container, 2... Granular molded product, 3... Supply port, 4... Discharge port, 5... Horizontal rotating shaft, 6... Receiver, 7... Storage tank, 8... Input port, 9... Discharge gate rotating shaft, 10... Discharge gate, 11... Vertical shaft, 12... Connecting plate, 21... Storage tank, 22...
- Sub-hopper, 23... Opening/closing gate, 24... Gate rotation axis, 25... Discharge gate rotation axis, 26... Discharge gate.

Claims (3)

【特許請求の範囲】[Claims] (1)微細粒子を水和塩成長反応を用いて粒状固体に成
形固化して排出するための貯留装置であって、 水和塩形成物質を含む微細粒子を加湿成形 した粒状成形品の供給口を上部に有し、下部に排出口を
有し、さらに内部に前記供給口に供給される粒状成形品
を受けかつ水平回転軸により回転可能たらしめた受け皿
を備えた受け容器と、 上部に投入口を有し、かつ排出機構を備え た貯留部とからなり、 前記受け容器をその排出口が前記貯留部の 投入口に連通可能に配設し、前記受け皿の回転により受
け皿上の粒状成形品が前記貯留部内に落下する如く構成
したことを特徴とする貯留装置。
(1) A storage device for molding and solidifying fine particles into granular solids using a hydrated salt growth reaction and discharging them, the supply port for granular molded products obtained by humidifying and molding fine particles containing hydrated salt-forming substances. a receiving container having an upper part, a discharge port at a lower part, and a receiving tray inside which receives a granular molded product supplied to the supply port and is rotatable by a horizontal rotation shaft; a storage part having a mouth and a discharge mechanism, the receiving container is arranged so that its discharge port can communicate with the input port of the storage part, and the granular molded product on the receiving tray is removed by rotation of the receiving tray. A storage device characterized in that the storage device is configured such that the particles fall into the storage section.
(2)前記受け皿が、回転傾斜時に前記粒状成形品の前
記貯留部への投入シュートとなるように形成されている
ものである特許請求の範囲第1項記載の貯留装置。
(2) The storage device according to claim 1, wherein the receiving tray is formed so as to serve as a chute for introducing the granular molded product into the storage section when the granular molded product is rotated and tilted.
(3)前記受け容器がほぼ中心の垂直軸を中心に回転し
、各回転位置に前記貯留部が複数個配置されているもの
である特許請求の範囲第1項又は第2項記載の貯留装置
(3) The storage device according to claim 1 or 2, wherein the receiving container rotates around a substantially central vertical axis, and a plurality of the storage portions are arranged at each rotational position. .
JP61228421A 1986-09-29 1986-09-29 Storage apparatus Granted JPS6384628A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61228421A JPS6384628A (en) 1986-09-29 1986-09-29 Storage apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61228421A JPS6384628A (en) 1986-09-29 1986-09-29 Storage apparatus

Publications (2)

Publication Number Publication Date
JPS6384628A true JPS6384628A (en) 1988-04-15
JPH0543413B2 JPH0543413B2 (en) 1993-07-01

Family

ID=16876209

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61228421A Granted JPS6384628A (en) 1986-09-29 1986-09-29 Storage apparatus

Country Status (1)

Country Link
JP (1) JPS6384628A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55161889U (en) * 1979-05-07 1980-11-20
JPS59128132A (en) * 1983-01-08 1984-07-24 Hitachi Plant Eng & Constr Co Ltd Rotary valve

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55161889U (en) * 1979-05-07 1980-11-20
JPS59128132A (en) * 1983-01-08 1984-07-24 Hitachi Plant Eng & Constr Co Ltd Rotary valve

Also Published As

Publication number Publication date
JPH0543413B2 (en) 1993-07-01

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