JPS6042872B2 - Granular material heating device - Google Patents

Granular material heating device

Info

Publication number
JPS6042872B2
JPS6042872B2 JP4520976A JP4520976A JPS6042872B2 JP S6042872 B2 JPS6042872 B2 JP S6042872B2 JP 4520976 A JP4520976 A JP 4520976A JP 4520976 A JP4520976 A JP 4520976A JP S6042872 B2 JPS6042872 B2 JP S6042872B2
Authority
JP
Japan
Prior art keywords
heating
wind box
heating tower
heating device
metal plate
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.)
Expired
Application number
JP4520976A
Other languages
Japanese (ja)
Other versions
JPS52127433A (en
Inventor
滋喜 大歯
重彌 柳瀬
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.)
SHOWA TETSUKO KK
Original Assignee
SHOWA TETSUKO KK
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 SHOWA TETSUKO KK filed Critical SHOWA TETSUKO KK
Priority to JP4520976A priority Critical patent/JPS6042872B2/en
Publication of JPS52127433A publication Critical patent/JPS52127433A/en
Publication of JPS6042872B2 publication Critical patent/JPS6042872B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は鋳物砂等の粒状物の加温装置に関するものであ
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heating device for granular materials such as foundry sand.

鋳物業界において、白砂性鋳型の採用が多くなつた。In the foundry industry, white sand molds are increasingly being used.

白砂性鋳型は粘結剤(有機、無機の粘結剤が使。White sand molds use binders (organic and inorganic binders).

用される)と硬化剤との化学反応により白砂するもので
ある。この化学反応は気温、並びに砂温等の影響を受け
やすく高温の鋳物砂を使用した場合には、反応速度が早
過ぎて造型が困難になり、反対に砂の温度が低過ぎる場
合には、反応速度が遅くなり、硬化するまでに時間がか
)り過ぎるとか、粘結剤と硬化剤の使用量が多くなると
かの問題が発生していた。このような問題点の内の高温
砂を効果的に冷却する為に、発明者らは加熱粒状物の冷
却装置(特願昭第50−77391号)を提案した。
It produces white sand through a chemical reaction between the hardening agent and the hardening agent. This chemical reaction is affected by air temperature and sand temperature, so if high temperature foundry sand is used, the reaction rate will be too fast and molding will be difficult; on the other hand, if the sand temperature is too low, Problems have arisen in that the reaction rate is slow, it takes too much time to cure, and the amount of binder and curing agent used is large. In order to effectively cool down the high-temperature sand due to these problems, the inventors proposed a cooling device for heated granules (Japanese Patent Application No. 77391/1982).

本発明は、砂の温度が低過ぎる場合の欠点を解″消する
ために、砂を加温塔内に均一に分散させて落下させ対向
流であるところの温風と1粒1粒の砂粒を完全かつ均一
に接触させることにより、効果的な加温を行うようにし
たもので、構造簡単な加温装置を提供することを目的と
する。
In order to solve the drawbacks when the temperature of the sand is too low, the present invention is designed to uniformly disperse the sand in a heating tower and drop it, and to separate each grain of sand from the counterflow of warm air. The purpose of the present invention is to provide a heating device with a simple structure, which performs effective heating by bringing the objects into complete and uniform contact with each other.

次に本発明に係る粒状物の加温装置の具体的構成を図面
について詳細に説明する。
Next, the specific configuration of the granular material heating device according to the present invention will be explained in detail with reference to the drawings.

第1図および第2図は本発明の第1の実施例を示したも
ので、加温塔1はフレーム(図示せず)により基礎面上
に直立に支持設置してある。
1 and 2 show a first embodiment of the present invention, in which a heating tower 1 is supported and installed upright on a foundation surface by a frame (not shown).

該加温塔1の上部には鋳物砂等の粒状物の投入口2を設
け、下部は円すい状となしその底部に排出用バルブ11
を設けてある。温風は吸入口6から風箱3内に設けたパ
ンチングメタル(多数の小孔を打ち抜いた有孔金属板)
10の小孔を通り加温塔内に導かれ加温塔内で粒状物と
熱交換し加温塔上部に形成した風箱3内に入りパンチン
グメタル10内の小孔を通り、排気口4より排風機(図
示せず)を通つて排気される。
The upper part of the heating tower 1 is provided with an inlet 2 for granular materials such as foundry sand, and the lower part is conical and a discharge valve 11 is provided at the bottom.
is provided. Hot air is supplied from the intake port 6 through a punching metal (perforated metal plate with many small holes punched out) installed inside the wind box 3.
It is led into the heating tower through the small hole 10, exchanges heat with the granules in the heating tower, enters the wind box 3 formed at the top of the heating tower, passes through the small hole in the punched metal 10, and is led to the exhaust port 4. The air is then exhausted through an exhaust fan (not shown).

一方鋳物砂等の粒状物は加温塔最上部に張設したパンチ
ングメタル7の小孔(孔の径は少なくとも3WLφ以上
が必要)を通り雨状になつてその下のパンチングメタル
8−1の面上に落下し跳ね返りながら小孔を通過しさら
に下のパンチングメタル8−2,8−3と適当数設けた
パンチングメタルを通過する間に粒状物は加温塔1内に
均一に分散し落下し、対向流であるところの温風と個々
の粒子が均一かつ完全に接触するから、効果的な加温が
可能である。加温された粒状物は加温塔の底部に溜り排
出バルブ11より排出される。なお各パンチングメタル
間の間隔は少なくとも150w1n以上とし、粒状物に
落下加速度を支えるようにすると分散が良好であつた。
又加温塔下部の温風吸入側に風箱5並びに風箱内にパン
チングメタル10を設けたのは吸入口6から入つた温風
はパンチングメタルが抵抗になり風箱全体に空気がまわ
り加温塔の全周から温風が導入できる効果がある。さら
に排気側の風箱3で加温塔の断面積が大きくなり、風速
が遅くなるので、粒状物を排気側に引き込むことがなく
、加温塔内での風速を一層速くすることができる。こ)
で風速をより速くできるということは加温効率が高くな
ることを意味している。また、排風側の風箱3内にパン
チングメタル9のスクリーンを設けたのは、前述した吸
入側のパンチングメタル10と同様の効果により加温塔
の全周から空気を排気し、加温塔内での空気の流れを均
一にすることができるものである。
On the other hand, granular materials such as foundry sand pass through the small holes (the diameter of the holes must be at least 3WLφ or more) in the punching metal 7 stretched at the top of the heating tower, and form rain on the surface of the punching metal 8-1 below. The granules fall upward, bounce back and pass through the small hole, and then pass through the punching metals 8-2, 8-3 and an appropriate number of punching metals below, while the particles are uniformly dispersed in the heating tower 1 and fall. Effective heating is possible because the individual particles come into uniform and complete contact with the hot air flowing in opposite directions. The heated granules accumulate at the bottom of the heating tower and are discharged from the discharge valve 11. Note that dispersion was good when the distance between each punching metal was at least 150 w1n or more and the falling acceleration was supported by the granules.
Also, the reason why a wind box 5 and a punching metal 10 are installed inside the wind box on the hot air intake side at the bottom of the heating tower is that the punching metal acts as a resistance to the hot air entering from the intake port 6, and the air circulates around the entire wind box. This has the effect of introducing hot air from all around the heating tower. Furthermore, since the cross-sectional area of the heating tower is increased in the wind box 3 on the exhaust side and the wind speed is reduced, particulate matter is not drawn into the exhaust side, and the wind speed within the heating tower can be further increased. child)
Being able to increase the wind speed means higher heating efficiency. In addition, a screen made of punched metal 9 is provided in the wind box 3 on the exhaust side, which has the same effect as the punched metal 10 on the suction side described above, and allows air to be exhausted from the entire circumference of the heating tower. This allows for even air flow inside.

次に第3図および第4図に示す第2実施例について説明
する。
Next, a second embodiment shown in FIGS. 3 and 4 will be described.

この実施例においては前記第1実施例に示した構成の加
温塔内に新たにパンチングメタル12を設けたもので、
パンチングメタル12の効果は加温塔上部のパンチング
メタル8で加温塔内に雨だれ状に均一に分散されて落下
した粒状物は先ずパンチングメタル12−1の面上で跳
ね飛ばされながら、パンチングメタルの小孔を通過して
、順次下段のパンチングメタルの面上に落下する。
In this embodiment, a punching metal 12 is newly installed in the heating tower having the configuration shown in the first embodiment.
The effect of the punching metal 12 is that the granules that fall are uniformly dispersed in the shape of raindrops inside the heating tower by the punching metal 8 at the top of the heating tower, are first splashed off on the surface of the punching metal 12-1, and then the punched metal It passes through the small hole and falls one after another onto the surface of the punched metal at the bottom.

従つて、第1実施例に比ベパンチングメタル12を設け
たことにより、粒状物の加温塔内で滞留時間は長くなる
と共に、パンチングメタル間の間隔を150WI1L以
上にすればパンチングメタル面上での粒状物の跳躍現象
が発生するので、砂の層ができることもなく、粒状物の
一層完全な加温ができる。また加温塔内を通過する空気
は、パンチングメタル12の部分で断面積が小さくなり
流速を増すので加温効果を一層増すことが期待できる。
こ)でパンチングメタル12の段数は、必要に応じて決
定されるもので、第3図に示した5段は1例にすぎない
ことは言うまでもない。パンチングメタルの形状は、単
に金属板に小孔を打ち抜いたものでもよいが、第4図に
示したパンチングメタルの一部拡大図のように、下側を
押し広げた形状にフレアー加工したものを使用すれば空
気抵抗を少なくすることができる。
Therefore, compared to the first embodiment, by providing the punching metal 12, the residence time of the granules in the heating tower becomes longer, and if the interval between the punching metals is set to 150 WI 1L or more, it is possible to increase the retention time on the punching metal surface. Since a jumping phenomenon of the granules occurs, a layer of sand is not formed, and the granules can be heated more completely. In addition, the cross-sectional area of the air passing through the heating tower becomes smaller at the punched metal 12 and the flow velocity increases, so it can be expected that the heating effect will be further increased.
In this case, the number of stages of the punching metal 12 is determined as necessary, and it goes without saying that the five stages shown in FIG. 3 is just one example. The shape of the punched metal may be simply a metal plate with small holes punched out, but as shown in the partially enlarged view of the punched metal shown in Figure 4, it is possible to form a punched metal with a flared shape that stretches the bottom side. It can be used to reduce air resistance.

こ)で空気は矢印の方向に通過する。第5図に示したも
のは本発明の第3実施例で前記第1および第2実施例の
構成に、排風機を兼ねた収塵機13、熱交換器15(ア
ルミフィンコイル)、熱媒加熱機16(ボイラー)、並
びにそれらを接続するダクト4″,6″,14、熱媒を
循環するバイブ17を装備したものである。
Air passes in the direction of the arrow. FIG. 5 shows a third embodiment of the present invention, which has the same structure as the first and second embodiments, but includes a dust collector 13 that also serves as an exhaust fan, a heat exchanger 15 (aluminum fin coil), and a heat medium. It is equipped with a heating device 16 (boiler), ducts 4'', 6'', and 14 that connect them, and a vibrator 17 that circulates a heat medium.

なお排風機を兼ねた収塵機13にサイクロン式のものを
図示したが、その他の一般的収塵機でも良い。
Although a cyclone type dust collector 13 which also serves as an exhaust fan is shown in the figure, other general dust collectors may be used.

収塵機13より送り出された空気はダクト14を通り、
加熱装置16から送られた熱媒により加熱された熱交換
器15を通過する間に強制加熱されて温風となる。
The air sent out from the dust collector 13 passes through the duct 14,
While passing through the heat exchanger 15 heated by the heat medium sent from the heating device 16, the air is forcibly heated and becomes warm air.

温風はダクト6″、風箱5を通り加熱塔1内に入り、上
部より落下する粒状物を加温し、風箱3、ダクト4″を
通つて収塵機13に入り粉塵と空気は分離され空気は再
循環され“る。この実施例では温風は強制的に加熱され
て作られるので、加温塔内を通過する粒状物は容易に適
温にまで加温されるものである。以上本発明に係る粒状
物の加温装置によれば、加温塔内を粒状物は、雨だれ状
に均一に分散され.た状態で落下するので、対向流であ
る温風による加温効果は大幅に向上する。
The warm air enters the heating tower 1 through the duct 6'' and the wind box 5, heats the granules falling from the top, and enters the dust collector 13 through the wind box 3 and the duct 4'', where the dust and air are removed. The separated air is recirculated. In this embodiment, the hot air is forcibly heated, so that the particulate matter passing through the heating tower is easily heated to an appropriate temperature. As described above, according to the granular material heating device according to the present invention, the granular materials fall in the heating tower in a uniformly dispersed state in the form of raindrops, so that the heating effect of the counterflow of hot air is reduced. Significantly improved.

また加温塔内に数段に渉つて設けたパンチングメタルの
効果によつて粒状物は分散した状態で、加温塔内での滞
留時間を長くすることができる。この面からも加温効果
jを向上できる。さらに本発明の加温装置には、加温塔
内に可動部分が無いので保持が容易であり、鋳物砂等の
粒状物の加温装置として有効である。
Further, due to the effect of the punching metal provided in several stages within the heating tower, the particulate matter is kept in a dispersed state, and the residence time within the heating tower can be extended. From this aspect as well, the heating effect j can be improved. Furthermore, since the heating device of the present invention has no movable parts in the heating tower, it is easy to maintain and is effective as a heating device for granular materials such as foundry sand.

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

第1図は本発明に係る粒状物の加温装置の第1の実施例
を示す断面図、第2図は加温装置の正面図、第3図は第
2実施例を示す断面図、第4図は同上のパンチングメタ
ルの一例を示す一部の拡大断面図、第5図は第3実施例
の正面図である。 1・・・・・・加温塔、2・・・・・・取入口、3,5
・・・・・・風箱、4・・・・・・排気口、4″,6″
・・・・・・ダクト、8・・・・パンチングメタル、1
3・・・・・収塵機、14・・・・・・ダクト、15・
・・・・・熱交換機、16・・・・・・熱媒加熱機、1
7・・・・・熱媒循環バイブ。
FIG. 1 is a sectional view showing a first embodiment of a granular material heating device according to the present invention, FIG. 2 is a front view of the heating device, and FIG. 3 is a sectional view showing a second embodiment. FIG. 4 is a partially enlarged sectional view showing an example of the punched metal same as above, and FIG. 5 is a front view of the third embodiment. 1...Heating tower, 2...Intake port, 3,5
...Wind box, 4...Exhaust port, 4″, 6″
...Duct, 8...Punching metal, 1
3...Dust collector, 14...Duct, 15.
... Heat exchanger, 16 ... Heat medium heating machine, 1
7... Heat medium circulation vibe.

Claims (1)

【特許請求の範囲】 1 直立して設置された加温塔の上部に粒状物の取入口
を、下部に排出バルブを設ける一方、空気取入口を有し
、かつ小孔を多数打ち抜いた有孔金属板を内蔵した風箱
を下部に、また有孔金属板を内装し、排気口を有する風
箱を上部に設け、加温塔内で風箱と取入口との間に粒状
物を分散させるための小孔を多数打ち抜いた有孔金属板
を、適当な間隔をおいて適宜の段数設けたことを特徴と
する粒状物の加温装置。 2 加温塔内において上位風箱と下位風箱との間に粒状
物の落下速度を制御するための小孔を多数打ち抜いた有
孔金属板を、適当な間隔をおいて適宜の段数設けたこと
を特徴とする特許請求の範囲第1項記載の粒状物の加温
装置。 3 収塵機、熱交換機、熱媒加熱機をダクト、並びに熱
媒循還パイプで加温塔に接続したことを特徴とする特許
請求の範囲第1項または第2項のいずれかに記載の粒状
物の加温装置。
[Scope of Claims] 1. A heating tower installed upright has a granular material intake in the upper part and a discharge valve in the lower part, and has an air intake and a large number of small holes punched out. A wind box with a built-in metal plate is installed at the bottom, and a wind box with a perforated metal plate inside and an exhaust port is installed at the top, and particulate matter is dispersed between the wind box and the intake in the heating tower. A heating device for granular materials, characterized in that a perforated metal plate having a large number of small holes punched therein is provided with an appropriate number of stages at appropriate intervals. 2 In the heating tower, between the upper wind box and the lower wind box, a perforated metal plate with a large number of small holes punched out to control the falling speed of particulate matter was provided in an appropriate number at appropriate intervals. A heating device for granular materials according to claim 1, characterized in that: 3. The device according to claim 1 or 2, characterized in that a dust collector, a heat exchanger, and a heat medium heater are connected to a heating tower through a duct and a heat medium circulation pipe. Granular material heating device.
JP4520976A 1976-04-20 1976-04-20 Granular material heating device Expired JPS6042872B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4520976A JPS6042872B2 (en) 1976-04-20 1976-04-20 Granular material heating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4520976A JPS6042872B2 (en) 1976-04-20 1976-04-20 Granular material heating device

Publications (2)

Publication Number Publication Date
JPS52127433A JPS52127433A (en) 1977-10-26
JPS6042872B2 true JPS6042872B2 (en) 1985-09-25

Family

ID=12712864

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4520976A Expired JPS6042872B2 (en) 1976-04-20 1976-04-20 Granular material heating device

Country Status (1)

Country Link
JP (1) JPS6042872B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0515024Y2 (en) * 1987-03-06 1993-04-21

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0515024Y2 (en) * 1987-03-06 1993-04-21

Also Published As

Publication number Publication date
JPS52127433A (en) 1977-10-26

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