JP2014195756A - Nozzle device for molding viscous material and band-type drying apparatus with the same - Google Patents

Nozzle device for molding viscous material and band-type drying apparatus with the same Download PDF

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JP2014195756A
JP2014195756A JP2013071764A JP2013071764A JP2014195756A JP 2014195756 A JP2014195756 A JP 2014195756A JP 2013071764 A JP2013071764 A JP 2013071764A JP 2013071764 A JP2013071764 A JP 2013071764A JP 2014195756 A JP2014195756 A JP 2014195756A
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nozzle
viscous material
cross
band
nozzle body
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JP6235223B2 (en
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真人 山口
Masato Yamaguchi
真人 山口
佳人 礒部
Yoshihito Isobe
佳人 礒部
信義 後藤
Nobuyoshi Goto
信義 後藤
山本 誠
Makoto Yamamoto
山本  誠
威喜 松井
Takeyoshi Matsui
威喜 松井
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JFE Engineering Corp
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Abstract

PROBLEM TO BE SOLVED: To obtain a nozzle device for molding viscous materials in which the viscous materials pass at the uniform flow rate in a width direction in a nozzle and equal molding is made, and a band-type drying apparatus with the device.SOLUTION: A nozzle device 1 for molding viscous materials concerning the present invention has: a cylindrical nozzle body 5 of a rectangular cross section, having a discharge port 5b at one end, and having a charging hole 5a of the viscous materials at the other end; and a header part 7 with one side connected to the charging hole 5a in the nozzle body 5, and with the other side connected to transport piping for transporting the viscous materials. The header part 7 is set such that a cross section Sof the connection part with the charging hole 5a of the nozzle body 5 is larger than the cross section Sof the connection part with the transport piping, and the viscous materials supplied from the transport piping are made to stay temporarily at the header part 7, and thereby the viscous materials are spread and supplied in the width direction of the nozzle body 5.

Description

本発明は、汚泥(特に下水汚泥)、畜糞、食品残渣、食品、化成品、肥料等の粘性物質を成形するために用いる粘性物質成形用ノズル装置及びバンド式乾燥装置に関するものである。   The present invention relates to a viscous material forming nozzle device and a band-type drying device used for forming viscous materials such as sludge (especially sewage sludge), livestock dung, food residues, foods, chemical products, and fertilizers.

粘性物質、例えば汚泥の有効利用を図る目的で、汚泥を成形して乾燥する多段バンド式汚泥乾燥装置が例えば特許文献1に提案されている。
特許文献1に提案された多段バンド式汚泥乾燥装置においては、汚泥貯留槽から汚泥輸送ポンプによって脱水汚泥を成形ノズルに供給して棒状に成形し、成形された成形汚泥を乾燥するようにしている。
For example, Patent Document 1 proposes a multi-stage band-type sludge drying apparatus that forms and dries sludge for the purpose of effectively using a viscous substance, such as sludge.
In the multi-band type sludge drying apparatus proposed in Patent Document 1, dehydrated sludge is supplied from a sludge storage tank to a forming nozzle by a sludge transport pump and formed into a rod shape, and the formed formed sludge is dried. .

特許文献1においては、成形ノズルとして、「粘着性材料を輸送する輸送配管に接続される末広ノズルからなる粘着性材料用成形ノズルであって、前記輸送配管と末広ノズルの接続部における末広ノズルの流路断面積が、末広ノズルの流出口における末広ノズルの流路断面積の40〜200%となっていることを特徴とする粘着性材料用成形ノズル。」(特許文献1の請求項1参照)が提案されている。   In Patent Document 1, as a forming nozzle, “a forming nozzle for an adhesive material composed of a divergent nozzle connected to a transport pipe for transporting an adhesive material, wherein the divergent nozzle at the connection between the transport pipe and the divergent nozzle is used. The flow channel cross-sectional area is 40 to 200% of the flow path cross-sectional area of the divergent nozzle at the outlet of the divergent nozzle. ”(Claim 1 of Patent Document 1) ) Has been proposed.

そして、粘性材料用成形ノズルに上記の構成を採用することでノズル内において偏流を生ずることなく均一な流速で粘性材料を、ノズル内を通過させることができ、円滑に成形できるとしている。   By adopting the above configuration for the viscous material molding nozzle, the viscous material can be passed through the nozzle at a uniform flow rate without causing a drift in the nozzle, and can be molded smoothly.

特開2012−5932号公報JP 2012-5932 A

しかしながら、特許文献1の粘着性材料用成形ノズルにおいては、輸送配管を末広ノズルに直接連結している。そのため、末広ノズルに供給された粘性材料が末広ノズルの幅方向に十分広がることができず、その結果、ノズル内おける通流速度が均一にならず、末広ノズルの出口においては、末広ノズルの中央部から粘性材料が速く吐出されるという現象が生じていた。   However, in the adhesive material molding nozzle of Patent Document 1, the transport pipe is directly connected to the divergent nozzle. Therefore, the viscous material supplied to the divergent nozzle cannot spread sufficiently in the width direction of the divergent nozzle, and as a result, the flow rate in the nozzle is not uniform, and at the outlet of the divergent nozzle, the center of the divergent nozzle There was a phenomenon that viscous material was quickly discharged from the part.

本発明はかかる課題を解決するためになされたものであり、ノズル内の幅方向において粘性物質が均一な流速で通過して、均等な成形ができる粘性物質成形用ノズル装置及び該装置を備えたバンド式乾燥装置を得ることを目的としている。   The present invention has been made in order to solve such a problem, and includes a viscous material molding nozzle device that can perform uniform molding by allowing a viscous material to pass at a uniform flow rate in the width direction of the nozzle, and the device. The purpose is to obtain a band-type dryer.

(1)本発明に係る粘性物質成形用ノズル装置は、一端に排出口を有し、他端に粘性物質の装入口を有する矩形断面の筒状のノズル本体と、一端側が前記ノズル本体における前記装入口に連結され、他端側が粘性物質を輸送する輸送配管に連結されたヘッダ部とを有し、
前記ヘッダ部は、前記ノズル本体の装入口との接続部の断面積が輸送配管との接続部の断面積よりも大きく設定されており、
前記輸送配管から供給された粘性物質を前記ヘッダ部で一時的に滞留させることで前記ノズル本体の幅方向へ粘性物質が広がって供給されるようにしたことを特徴とするものである。
(1) A viscous material forming nozzle device according to the present invention includes a cylindrical nozzle body having a rectangular cross section having a discharge port at one end and an inlet for a viscous material at the other end, and the one end side of the nozzle body in the nozzle body. A header portion connected to the loading port, the other end side being connected to a transport pipe for transporting the viscous material,
The header portion is set such that the cross-sectional area of the connection portion with the inlet of the nozzle body is larger than the cross-sectional area of the connection portion with the transport pipe,
The viscous substance supplied from the transport pipe is temporarily retained in the header portion so that the viscous substance is spread and supplied in the width direction of the nozzle body.

(2)また、上記(1)に記載のものにおいて、前記ヘッダ部におけるノズル本体の装入口との接合部の断面積が、ノズル本体の装入口の断面と一致していることを特徴とするものである。 (2) Further, in the above (1), the cross-sectional area of the joint portion of the header portion with the nozzle body inlet is coincident with the section of the nozzle body inlet. Is.

(3)また、上記(1)又は(2)に記載のものにおいて、前記ヘッダ部における前記装入口との接合部の断面積が、前記ヘッダ部における前記輸送配管との接合部の断面積の2倍〜10倍に設定されていることを特徴とするものである。 (3) In the above (1) or (2), the cross-sectional area of the joint portion of the header portion with the loading port is the cross-sectional area of the joint portion of the header portion with the transport pipe. It is characterized by being set to 2 to 10 times.

(4)また、上記(1)乃至(3)のいずれかに記載のものにおいて、前記ノズル本体における成形流路に、流路幅方向両側よりも中央部の流路を狭くする流路規制板を設けたことを特徴とするものである。 (4) Further, in any of the above (1) to (3), the flow path regulating plate that narrows the flow path in the central portion of the molding flow path in the nozzle body than the both sides in the flow path width direction. Is provided.

(5)本発明に係るバンド式乾燥装置は、乾燥装置本体の内部に被乾燥物である粘性物質を搬送するバンドを備え、バンドによって搬送される粘性物質を温風で乾燥するバンド式乾燥装置であって、
粘性物質が装入される装入口に上記(1)乃至(4)のいずれかに記載の粘性物質成形用ノズル装置を備えてなることを特徴とするものである。
(5) A band-type drying apparatus according to the present invention includes a band for transporting a viscous material, which is an object to be dried, inside the drying apparatus body, and the viscous material transported by the band is dried with warm air. Because
The viscous material forming nozzle device according to any one of the above (1) to (4) is provided at a charging port into which the viscous material is charged.

本発明においては、ノズル本体の装入口にヘッダ部を設けることによって、輸送配管から供給された粘性物質をヘッダ部で一時的に滞留させることで、ノズル内の幅方向において粘性物質が均一な流速で通過して、均等な成形ができる。   In the present invention, by providing a header part at the inlet of the nozzle body, the viscous substance supplied from the transport pipe is temporarily retained in the header part, so that the viscous substance has a uniform flow rate in the width direction in the nozzle. Passing through, uniform molding is possible.

本発明の実施の形態1に係る粘性物質成形用ノズル装置の説明図である。It is explanatory drawing of the nozzle apparatus for viscous substance shaping | molding which concerns on Embodiment 1 of this invention. 本発明の実施の形態1に係る粘性物質成形用ノズル装置の平面図である。It is a top view of the nozzle apparatus for viscous material shaping | molding which concerns on Embodiment 1 of this invention. 本発明の実施の形態1の他の態様に使用する流路規制板の説明図である。It is explanatory drawing of the flow-path control board used for the other aspect of Embodiment 1 of this invention. 本発明の実施の形態1に係る粘性物質成形用ノズル装置の他の態様の説明図である。It is explanatory drawing of the other aspect of the nozzle apparatus for viscous substance shaping | molding which concerns on Embodiment 1 of this invention. 本発明の実施の形態2に係るバンド式乾燥装置の全体構成を説明する説明図である。It is explanatory drawing explaining the whole structure of the band type drying apparatus which concerns on Embodiment 2 of this invention.

[実施の形態1]
本発明の一実施の形態に係る粘性物質成形用ノズル装置1は、一端に排出口5bを有し、他端に粘性物質の装入口5aを有する矩形断面の筒状のノズル本体5と、一端側がノズル本体5における装入口5aに連結され、他端側が粘性物質を輸送する輸送配管(図示なし)に連結されるヘッダ部7とを有するものである。
なお、粘性物質としては、汚泥(特に下水汚泥)、畜糞、食品残渣、食品、化成品、肥料等を想定している。
各構成を詳細に説明する。
[Embodiment 1]
A nozzle device 1 for forming a viscous material according to an embodiment of the present invention has a cylindrical nozzle body 5 having a rectangular cross section having a discharge port 5b at one end and an inlet 5a for a viscous material at the other end, and one end. The side is connected to the inlet 5a in the nozzle body 5, and the other end has a header portion 7 connected to a transport pipe (not shown) for transporting the viscous material.
In addition, as a viscous substance, sludge (especially sewage sludge), livestock dung, food residue, food, chemical products, fertilizer, etc. are assumed.
Each configuration will be described in detail.

<ノズル本体>
ノズル本体5は、図1に示すように、一端に排出口5bを有し、他端に粘性物質の装入口5aを有する矩形断面の筒状に形成されている。
ノズル本体5の内部には粘性物質が通流する断面が矩形のノズル流路が形成されている。ノズル流路の出口の近傍には、例えば複数の切断ピンなどが幅方向に設置され、通流する粘性物質が成形されるようにしてもよい。
<Nozzle body>
As shown in FIG. 1, the nozzle body 5 is formed in a cylindrical shape having a rectangular cross section having a discharge port 5 b at one end and a viscous material inlet 5 a at the other end.
A nozzle channel having a rectangular cross section through which a viscous substance flows is formed inside the nozzle body 5. In the vicinity of the outlet of the nozzle channel, for example, a plurality of cutting pins or the like may be installed in the width direction so that a viscous substance that flows is formed.

<ヘッダ部>
ヘッダ部7は、一端側がノズル本体5における装入口5aに連結され、他端側が粘性物質を輸送する輸送配管(図示なし)に連結される。ヘッダ部7における輸送配管との接合部には図1、図2に示すようにフランジ部7aが設けられている。
ヘッダ部7は、輸送配管から供給された粘性物質を一時的に滞留させることでノズル本体5の幅方向へ粘性物質が広がって供給されるようにしている。
<Header part>
One end of the header portion 7 is connected to the inlet 5a in the nozzle body 5, and the other end is connected to a transport pipe (not shown) for transporting the viscous material. As shown in FIGS. 1 and 2, a flange portion 7 a is provided at a joint portion of the header portion 7 with the transport pipe.
The header portion 7 temporarily supplies the viscous material supplied from the transport pipe so that the viscous material spreads in the width direction of the nozzle body 5 and is supplied.

ヘッダ部7における装入口5aとの接合部の断面積S1(図1において破線で囲んだ部分の面積)は、ヘッダ部7における輸送配管との接合部の断面積S2の2倍〜10倍に設定するのが好ましい。このようにすることで、輸送配管から供給された粘性物質がヘッダ部7内で幅方向に広がるのを効果的に実現できる。 The cross-sectional area S 1 (the area of the portion surrounded by the broken line in FIG. 1) of the joint portion with the loading port 5a in the header portion 7 is 10 to 10 times the cross-sectional area S 2 of the joint portion with the transport pipe in the header portion 7. It is preferable to set to double. By doing in this way, it can implement | achieve effectively that the viscous substance supplied from transport piping spreads in the width direction within the header part 7. FIG.

また、図1に示すように、ヘッダ部7におけるノズル本体5の装入口5aとの接合部の断面積が、ノズル本体5の装入口5aの断面積と一致するようにするのが好ましい。
このようにすることで、ヘッダ部7内で幅方向に広がった粘性物質がそのままノズル本体5の全幅に亘って供給されるので、ノズル本体5内の流路粘性性物質が幅方向で均等な速度で降下することを効果的に実現できる。
Further, as shown in FIG. 1, it is preferable that the cross-sectional area of the joint portion of the header portion 7 with the inlet 5 a of the nozzle body 5 coincides with the sectional area of the inlet 5 a of the nozzle body 5.
By doing in this way, since the viscous substance spreading in the width direction in the header portion 7 is supplied as it is over the entire width of the nozzle body 5, the flow path viscous substance in the nozzle body 5 is even in the width direction. It is possible to effectively descend at a speed.

なお、ヘッダ部7の形状を図1、図2に示すように平面視において台形状にした場合には、ヘッダ部7における輸送配管側からノズル本体5に至る辺部の傾斜角度θを30°〜60°に設定するのが好ましい。傾斜角度θを30°以上にすることで、ヘッダ部7における輸送配管からノズル本体5に至る距離を十分確保でき、ヘッダ部7内において粘性物質が幅方向へ十分に広がるようにできる。
なお、角度θを大きくすることでヘッダ部7の体積が増えるので、幅方向への広がりの観点からは問題ないが、装置が大型化するので、角度θは60°以下に設定するのが好ましい。
In addition, when the shape of the header part 7 is made trapezoidal in a plan view as shown in FIGS. 1 and 2, the inclination angle θ of the side part from the transport piping side to the nozzle body 5 in the header part 7 is set to 30 °. It is preferable to set it at ˜60 °. By setting the inclination angle θ to 30 ° or more, a sufficient distance from the transport pipe in the header portion 7 to the nozzle body 5 can be secured, and the viscous substance can be sufficiently spread in the width direction in the header portion 7.
In addition, since the volume of the header part 7 increases by increasing the angle θ, there is no problem from the viewpoint of spreading in the width direction. However, since the apparatus is enlarged, the angle θ is preferably set to 60 ° or less. .

上記のように構成された本実施の形態によれば、輸送配管から供給された粘性物質は、ヘッダ部7で一時的に滞留し、幅方向に広がりながらノズル本体5に供給される。粘性物質が幅方向に広がった状態でノズル本体5に供給されることで、粘性物質はノズル本体5の流路を幅方向で均等に通流することができ、ノズル本体5の幅方向で均等な成形が可能になる。   According to the present embodiment configured as described above, the viscous substance supplied from the transport pipe is temporarily retained in the header portion 7 and supplied to the nozzle body 5 while spreading in the width direction. By supplying the viscous material to the nozzle body 5 in a state of spreading in the width direction, the viscous material can flow through the flow path of the nozzle body 5 evenly in the width direction, and evenly in the width direction of the nozzle body 5. Molding becomes possible.

なお、ノズル本体5の流路幅が広い場合等、ノズル流路での幅方向への粘性物質の広がりをより促進するために、図3に示すような、流路規制板11をノズル本体5の流路の途中に挿入するようにしてもよい。
流路規制板11は、図3に示すように、開口部11aを有する矩形枠状の板材からなり、開口部11aは両幅方向の面積が大きく、中央部が小さくなっている。
In order to further promote the spread of the viscous material in the width direction in the nozzle flow path, such as when the flow path width of the nozzle main body 5 is wide, a flow path regulating plate 11 as shown in FIG. You may make it insert in the middle of this flow path.
As shown in FIG. 3, the flow path regulating plate 11 is made of a rectangular frame-shaped plate material having an opening 11a, and the opening 11a has a large area in both width directions and a small central portion.

流路規制板11を設置する場合には、図4に示すように、ノズル本体5の出口近傍に、流路規制板挿入部13を設け、流路規制板11を着脱可能にするのが好ましい。着脱可能にすることで、粘性物質の性状等によって、異なる開口部11aを有する流路規制板11を適宜選択して挿入することができ、流路の形状を最も好ましいものにすることができる。   When the flow path restriction plate 11 is installed, as shown in FIG. 4, it is preferable that a flow path restriction plate insertion portion 13 is provided in the vicinity of the outlet of the nozzle body 5 so that the flow path restriction plate 11 can be attached and detached. . By making it detachable, the flow path regulating plate 11 having different openings 11a can be appropriately selected and inserted depending on the properties of the viscous substance, and the shape of the flow path can be made most preferable.

[実施の形態2]
本実施の形態は、実施の形態1で用いた粘性物質成形用ノズル装置1を、汚泥33が装入される装入口20に設けたバンド式乾燥装置21に関するものである。
バンド式乾燥装置21は、図5に示すように、乾燥装置本体22内に装入された汚泥33を搬送する複数段のバンド(本例では、1段目バンド23と2段目バンド25)を備えている。
そして、汚泥貯留槽27から汚泥輸送ポンプ29によって汚泥輸送配管31から供給される汚泥33を、粘性物質成形用ノズル装置1を介して乾燥装置本体22内に装入するようにしている。
[Embodiment 2]
The present embodiment relates to a band-type drying device 21 in which the viscous material forming nozzle device 1 used in the first embodiment is provided at the inlet 20 into which the sludge 33 is inserted.
As shown in FIG. 5, the band-type drying device 21 has a plurality of bands (in this example, a first-stage band 23 and a second-stage band 25) that convey the sludge 33 charged in the drying apparatus body 22. It has.
And the sludge 33 supplied from the sludge transport pipe 31 from the sludge storage tank 27 by the sludge transport pump 29 is inserted in the drying apparatus main body 22 via the nozzle apparatus 1 for viscous substance shaping | molding.

乾燥装置本体22には、温風発生熱交換器35で未利用排熱などと熱交換された温風が送風され、1段目バンド23および2段目バンド25で搬送されている汚泥33を乾燥するようになっている。その際、汚泥33からの臭気をできるだけ抑制しながら乾燥するためには、温風の温度を170〜240℃に設定し、汚泥33の表面に固化膜を形成させるようにするのが好ましい。
なお、温風の大半は循環ファン37によって温風発生熱交換器35と乾燥装置本体22内を循環し、一部は空気導入ファン39によって大気から導入され、一部は図示しない排気処理装置によって排気される。
The drying apparatus main body 22 is supplied with warm air that has been heat-exchanged with unused exhaust heat or the like by the hot-air generating heat exchanger 35, and sludge 33 that is conveyed by the first-stage band 23 and the second-stage band 25. It is supposed to dry. At that time, in order to dry while suppressing the odor from the sludge 33 as much as possible, it is preferable to set the temperature of the hot air to 170 to 240 ° C. and form a solidified film on the surface of the sludge 33.
Note that most of the hot air is circulated in the hot air generating heat exchanger 35 and the drying device main body 22 by the circulation fan 37, part is introduced from the atmosphere by the air introduction fan 39, and part is by the exhaust treatment device (not shown). Exhausted.

本実施の形態においては、粘性物質成形用ノズル装置1を介して汚泥33を乾燥装置本体22に供給するようにしたので、供給される汚泥33がバンド幅方向で均等になっており、効率的な乾燥ができる。   In the present embodiment, since the sludge 33 is supplied to the drying apparatus main body 22 via the viscous material forming nozzle device 1, the supplied sludge 33 is uniform in the bandwidth direction, which is efficient. Can be dried.

なお、本実施形態では、複数段のバンドを備えているが、本発明は、1段のみのバンドの場合にも同様に実施することができる。   In the present embodiment, a plurality of bands are provided. However, the present invention can be similarly implemented even in the case of only one band.

1 粘性物質成形用ノズル装置
5 ノズル本体
5a 装入口
5b 排出口
7 ヘッダ部
7a フランジ部
11 流路規制板
11a 開口部
13 流路規制板挿入部
20 装入口
21 バンド式乾燥装置
22 乾燥装置本体
23 1段目バンド
25 2段目バンド
27 汚泥貯留槽
29 汚泥輸送ポンプ
31 汚泥輸送配管
33 汚泥
35 温風発生熱交換器
37 循環ファン
39 空気導入ファン
DESCRIPTION OF SYMBOLS 1 Viscous material shaping | molding nozzle apparatus 5 Nozzle main body 5a Inlet 5b Outlet 7 Header part 7a Flange part 11 Flow path control board 11a Opening part 13 Flow path control board insertion part 20 Inlet 21 Band type dryer 22 Drying apparatus main body 23 First-stage band 25 Second-stage band 27 Sludge storage tank 29 Sludge transport pump 31 Sludge transport piping 33 Sludge 35 Hot air generating heat exchanger 37 Circulation fan 39 Air introduction fan

Claims (5)

一端に排出口を有し、他端に粘性物質の装入口を有する矩形断面の筒状のノズル本体と、一端側が前記ノズル本体における前記装入口に連結され、他端側が粘性物質を輸送する輸送配管に連結されたヘッダ部とを有し、
前記ヘッダ部は、前記ノズル本体の装入口との接続部の断面積が輸送配管との接続部の断面積よりも大きく設定されており、
前記輸送配管から供給された粘性物質を前記ヘッダ部で一時的に滞留させることで前記ノズル本体の幅方向へ粘性物質が広がって供給されるようにしたことを特徴とする粘性物質成形用ノズル装置。
A rectangular nozzle body having a discharge port at one end and a viscous material inlet at the other end, one end connected to the inlet in the nozzle body, and the other end transporting the viscous material A header connected to the pipe,
The header portion is set such that the cross-sectional area of the connection portion with the inlet of the nozzle body is larger than the cross-sectional area of the connection portion with the transport pipe,
A viscous material forming nozzle device characterized in that the viscous material supplied from the transport pipe is temporarily retained in the header portion so that the viscous material is spread and supplied in the width direction of the nozzle body. .
前記ヘッダ部におけるノズル本体の装入口との接合部の断面積が、ノズル本体の装入口の断面と一致していることを特徴とする請求項1記載の粘性物質成形用ノズル装置。   2. The nozzle device for forming a viscous material according to claim 1, wherein a cross-sectional area of a joint portion of the header portion with the inlet of the nozzle main body coincides with a cross section of the inlet of the nozzle main body. 前記ヘッダ部における前記装入口との接合部の断面積が、前記ヘッダ部における前記輸送配管との接合部の断面積の2倍〜10倍に設定されていることを特徴とする請求項1又は2に記載の粘性物質成形用ノズル装置。   The cross-sectional area of a joint portion between the header portion and the inlet is set to be 2 to 10 times the cross-sectional area of the joint portion between the header portion and the transport pipe. 2. The nozzle device for forming a viscous material according to 2. 前記ノズル本体における成形流路に、流路幅方向両側よりも中央部の流路を狭くする流路規制板を設けたことを特徴とする請求項1乃至3のいずれか一項に記載の粘性物質成形用ノズル装置。   The viscosity according to any one of claims 1 to 3, wherein a flow path regulating plate that narrows the flow path in the center portion than the both sides in the flow path width direction is provided in the molding flow path in the nozzle body. Nozzle device for material forming. 乾燥装置本体の内部に被乾燥物である粘性物質を搬送するバンドを備え、バンドによって搬送される粘性物質を温風で乾燥するバンド式乾燥装置であって、
粘性物質が装入される装入口に請求項1乃至4のいずれかに記載の粘性物質成形用ノズル装置を備えてなることを特徴とするバンド式乾燥装置。
A band-type drying device that includes a band for transporting a viscous material, which is an object to be dried, inside the drying device main body, and for drying the viscous material transported by the band with warm air,
A band-type drying apparatus comprising the viscous material forming nozzle device according to any one of claims 1 to 4 at a charging port into which a viscous material is charged.
JP2013071764A 2013-03-29 2013-03-29 Nozzle device for sludge molding and band-type drying device equipped with the device Active JP6235223B2 (en)

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JPH04158003A (en) * 1990-10-22 1992-06-01 Fuirutoreeshiyon Kk Polymer blender and manufacture thereof
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JPH0687615A (en) * 1992-09-02 1994-03-29 Nippon Sheet Glass Co Ltd Device for causing body to flow out from glass melting furnace
JPH07314445A (en) * 1994-05-16 1995-12-05 Renewed Materials Ind Inc Method and device for extrusion and extruded product thereby
WO1998001275A1 (en) * 1996-07-10 1998-01-15 Royal Ecoproducts Limited Process of making products from recycled material containing plastics
JP2002211934A (en) * 2000-11-10 2002-07-31 Ohara Inc Method of forming sheet glass
JP2008120667A (en) * 2006-10-20 2008-05-29 Ohara Inc Nozzle and method for producing optical glass gob using it
JP2009102200A (en) * 2007-10-24 2009-05-14 Ohara Inc Glass flow passage and method for manufacturing optical glass formed body using the same
JP2011173060A (en) * 2010-02-24 2011-09-08 Jfe Engineering Corp Nozzle for molding sludge and band-type sludge drying device
JP2011174654A (en) * 2010-02-24 2011-09-08 Jfe Engineering Corp Band type viscous substance drying device
JP2012005932A (en) * 2010-06-23 2012-01-12 Jfe Engineering Corp Forming nozzle for adhesive material, and band type drying device
JP2012024678A (en) * 2010-07-22 2012-02-09 Jfe Engineering Corp Nozzle for molding sludge, and band-type sludge drying device
JP2012512122A (en) * 2008-12-17 2012-05-31 モラフスキー,ミロスラフ Sheet glass manufacturing method and apparatus

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04158003A (en) * 1990-10-22 1992-06-01 Fuirutoreeshiyon Kk Polymer blender and manufacture thereof
JPH05256675A (en) * 1992-03-12 1993-10-05 Toshiba Corp Electromagnetic flowmeter
JPH0687615A (en) * 1992-09-02 1994-03-29 Nippon Sheet Glass Co Ltd Device for causing body to flow out from glass melting furnace
JPH07314445A (en) * 1994-05-16 1995-12-05 Renewed Materials Ind Inc Method and device for extrusion and extruded product thereby
WO1998001275A1 (en) * 1996-07-10 1998-01-15 Royal Ecoproducts Limited Process of making products from recycled material containing plastics
JP2002211934A (en) * 2000-11-10 2002-07-31 Ohara Inc Method of forming sheet glass
JP2008120667A (en) * 2006-10-20 2008-05-29 Ohara Inc Nozzle and method for producing optical glass gob using it
JP2009102200A (en) * 2007-10-24 2009-05-14 Ohara Inc Glass flow passage and method for manufacturing optical glass formed body using the same
JP2012512122A (en) * 2008-12-17 2012-05-31 モラフスキー,ミロスラフ Sheet glass manufacturing method and apparatus
JP2011173060A (en) * 2010-02-24 2011-09-08 Jfe Engineering Corp Nozzle for molding sludge and band-type sludge drying device
JP2011174654A (en) * 2010-02-24 2011-09-08 Jfe Engineering Corp Band type viscous substance drying device
JP2012005932A (en) * 2010-06-23 2012-01-12 Jfe Engineering Corp Forming nozzle for adhesive material, and band type drying device
JP2012024678A (en) * 2010-07-22 2012-02-09 Jfe Engineering Corp Nozzle for molding sludge, and band-type sludge drying device

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