JPS643978Y2 - - Google Patents
Info
- Publication number
- JPS643978Y2 JPS643978Y2 JP1984004417U JP441784U JPS643978Y2 JP S643978 Y2 JPS643978 Y2 JP S643978Y2 JP 1984004417 U JP1984004417 U JP 1984004417U JP 441784 U JP441784 U JP 441784U JP S643978 Y2 JPS643978 Y2 JP S643978Y2
- Authority
- JP
- Japan
- Prior art keywords
- granular
- particulate matter
- cylindrical body
- cylindrical
- preheated
- 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
Links
- 239000008187 granular material Substances 0.000 claims description 25
- 239000007789 gas Substances 0.000 claims description 17
- 239000000463 material Substances 0.000 claims description 17
- 239000013618 particulate matter Substances 0.000 claims description 17
- 238000005192 partition Methods 0.000 claims description 9
- 239000002912 waste gas Substances 0.000 claims description 9
- 239000011236 particulate material Substances 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 230000005855 radiation Effects 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 238000013341 scale-up Methods 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Crucibles And Fluidized-Bed Furnaces (AREA)
Description
【考案の詳細な説明】
〔産業上の利用分野〕
本考案は、粒状物を熱ガスを用いて効率よく予
熱する装置に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to an apparatus for efficiently preheating granular materials using hot gas.
従来、2枚のルーバ間に粒状物を充てんして移
動層を形成し、この移動層を熱交換器本体内に複
数個並列に配置した予熱装置が提案されている。
Conventionally, a preheating device has been proposed in which a moving layer is formed by filling a space between two louvers with granules, and a plurality of moving layers are arranged in parallel within a heat exchanger main body.
また実公昭35−33569号公報には、塔枠1内に
多孔壁を構成する二重筒体2を縦置きに配設し、
これら筒体2間に形成される資料(たとえば飼
料)通路5に対し、資料入口11に送風機17
を、資料出口12に排風機22を配設し、もつて
該通路内を自重により下方へ移動する資料を数回
にわたつて横切つて蛇行状に上方へ向う熱風通路
を設けてなる竪型乾燥機が記載されている。 Further, in Japanese Utility Model Publication No. 35-33569, a double cylinder body 2 forming a porous wall is arranged vertically within a tower frame 1,
A blower 17 is installed at the material entrance 11 for the material (for example, feed) passage 5 formed between these cylinders 2.
is a vertical type, in which an air exhaust fan 22 is disposed at the material exit 12, and a hot air passage is provided in which the material moves downward under its own weight in the passage several times and goes upward in a meandering manner. A dryer is listed.
上記の2枚のルーバ間に粒状物を充てんして移
動層を形成した予熱装置においては、(1)熱交換器
本体が角型、箱型のため、熱ガスの偏流が生じ、
設置スペースが大きくなる。(2)熱ガスと被予熱物
である粒状物が1回のみの接触のため、熱交換率
が低い。(3)ユニツト化されていないので、その都
度、設計する必要がある。(4)被予熱物である粒状
物の落下距離が一定でないため、予熱後温度にバ
ラツキがある。などの不都合がある。
In the preheating device described above in which a moving layer is formed by filling the space between the two louvers, (1) the heat exchanger body is rectangular or box-shaped, resulting in uneven flow of hot gas;
Installation space becomes larger. (2) The heat exchange rate is low because the hot gas and the granular material to be preheated come into contact only once. (3) Since it is not unified, it is necessary to design it each time. (4) Since the falling distance of the granular material to be preheated is not constant, the temperature after preheating varies. There are other inconveniences.
また上記の実公昭35−33569号公報記載の乾燥
機においては、熱ガスと被加熱物とが数回にわた
つて接触するという利点があるが、熱発生炉18
が乾燥機の外部に設けられ、熱風供給管16を介
して乾燥機に接続されているので、熱風供給管
(ダクト)16や炉体からの放熱損失があり、か
つコンパクト化および大容量への対応を図ること
が難しいという不都合がある。 Further, the dryer described in the above-mentioned Japanese Utility Model Publication No. 35-33569 has the advantage that the hot gas and the object to be heated come into contact with each other several times.
is provided outside the dryer and connected to the dryer via the hot air supply pipe 16, so there is heat radiation loss from the hot air supply pipe (duct) 16 and the furnace body, and it is difficult to downsize and increase the capacity. The problem is that it is difficult to take appropriate measures.
また被処理物抜出部が一箇所に集中しているの
で、被処理物に偏流が生じて抜き出し難い場合が
ある。 In addition, since the workpiece extracting portion is concentrated in one place, there may be a case where a drift occurs in the workpiece and it is difficult to extract the workpiece.
さらに遮断板7,8,10が水平であるので、
支持体(二重筒体)からこぼれた被処理物は堆積
したままになつているなどの不都合がある。 Furthermore, since the shielding plates 7, 8, and 10 are horizontal,
There are inconveniences such as the objects to be processed spilling from the support (double cylinder) remaining piled up.
本考案は上記の諸点を解決するためになされた
もので、熱ガス発生装置を本体内に組み込み、か
つ仕切板を傾斜した形状とし、さらに粒状予熱物
出口を複数個設けることにより、ダクトや熱ガス
発生装置からの放熱損失をなくし、コンパクト化
および大容量への対応を容易にすることができ、
かつ被処理物の抜出時の偏流を少なくし、支持体
からこぼれた被処理物が層内へ戻るようにした粒
状物の予熱装置を提供することを目的とするもの
である。 The present invention was developed to solve the above-mentioned problems, and by incorporating a hot gas generator into the main body, making the partition plate an inclined shape, and providing multiple outlets for granular preheated material, it is possible to It eliminates heat radiation loss from the gas generator, making it easier to downsize and handle large capacity.
Another object of the present invention is to provide a preheating device for granular materials that reduces drifting flow when the material to be processed is taken out and allows the material to be processed spilled from the support to return into the layer.
上記の目的を達成するために、本考案の粒状物
の予熱装置は、図面に示すように、上端に粒状物
入口2を有し、下端に粒状予熱物出口3を有し、
上側部に低温廃ガス出口4を有する円筒状本体1
内に、間隙8を有するように円筒状ルーバ10,
11を縦方向に二重に配設し、円筒状ルーバ間に
被予熱物である粒状物12を充てんして粒状物移
動層13を形成し、円筒状本体1内における粒状
物移動層13の上端に粒状物ホツパ14を接続し
た粒状物移動層式の予熱装置において、円筒状本
体1内の下部中央部に熱ガス発生装置7を組み込
み、熱ガス発生装置7の上側における粒状物移動
層13,13の間、低温廃ガス出口4の下側にお
ける粒状物移動層13と円筒状本体1との間に傾
斜した仕切板15,16を交互に配置し、下端の
粒状予熱物出口3を複数個配設したことを特徴と
している。
In order to achieve the above object, the granular material preheating device of the present invention has a granular material inlet 2 at the upper end, a granular preheating material outlet 3 at the lower end, as shown in the drawings,
Cylindrical body 1 with a cold waste gas outlet 4 in the upper part
a cylindrical louver 10 having a gap 8 therein;
11 are arranged in a double manner in the longitudinal direction, and the cylindrical louvers are filled with granular materials 12 as objects to be preheated to form a granular material moving layer 13. In a particulate material moving bed type preheating device having a particulate material hopper 14 connected to the upper end, a hot gas generator 7 is installed in the lower central part of the cylindrical body 1, and a particulate material moving layer 13 is installed above the hot gas generating device 7. , 13, inclined partition plates 15 and 16 are arranged alternately between the particulate material movement layer 13 and the cylindrical body 1 below the low-temperature waste gas outlet 4, and a plurality of particulate preheated material outlets 3 at the lower end are arranged. It is characterized by the fact that it is individually arranged.
被予熱物である粒状物は粒状物入口2から投入
され、一定速度で二重の円筒状ルーバ10,11
内を移動し、この間、熱ガス発生装置7から発生
した熱ガスが粒状物移動層13内を複数回流れ
て、粒状物を効率よく予熱する。予熱された粒状
物は複数の粒状予熱物出口3から偏流を生じるこ
となく円滑に取り出される。また仕切板15,1
6の上にこぼれ出た粒状物は、仕切板が傾斜して
いるので、ルーバの間から粒状物移動層13内に
自然に戻る。なお支持体として、ルーバを用いて
いるので、開口部が目詰まりすることはない。
The granular material to be preheated is introduced from the granular material inlet 2 and passed through the double cylindrical louvers 10 and 11 at a constant speed.
During this time, the hot gas generated from the hot gas generator 7 flows through the particulate matter moving layer 13 multiple times to efficiently preheat the particulate matter. The preheated granular material is smoothly taken out from the plurality of granular preheated material outlets 3 without causing drift. In addition, the partition plate 15,1
Since the partition plate is inclined, the particulate matter spilled onto the particulate matter movement layer 13 naturally returns between the louvers. Note that since a louver is used as the support, the opening will not become clogged.
以下、本考案の実施例を図面に基づいて説明す
る。1は保温材を被覆した円筒状本体で、この円
筒状本体1は上端に粒状物入口2を有し、下端に
複数個(図面では一例として4個)の粒状予熱物
出口3を有し、上側部に低温廃ガス出口4を有
し、下部中央部にバーナ5および燃焼室6からな
る熱ガス発生装置7を有している。この円筒状本
体1内に間隙8を有するように円筒状ルーバ1
0,11を縦方向に二重に配設し、円筒状ルーバ
10,11間に被予熱物である粒状物12を充て
んして粒状物移動層13を形成し、円筒状本体1
内において粒状物移動層13の上端に粒状物ホツ
パ14を接続する。さらに少なくとも熱ガス発生
装置7の上側における粒状物移動層13の間、低
温廃ガス出口4の下側における粒状物移動層13
と円筒状本体1との間に傾斜した仕切板15,1
6を交互に配置している。第1図においては、仕
切板を2段に設ける場合を示しているが、3段以
上とすることも可能である。円筒状の粒状物移動
層13の下部は複数個(図面では一例として4
個)の膨出部17に接続され、この膨出部17は
前記粒状予熱物出口3に接続されている。18は
廃ガスダクトである。
Hereinafter, embodiments of the present invention will be described based on the drawings. 1 is a cylindrical body covered with a heat insulating material, and this cylindrical body 1 has a granular material inlet 2 at the upper end, and a plurality of granular preheated material outlets 3 (four as an example in the drawing) at the lower end, It has a low-temperature waste gas outlet 4 in the upper part, and a hot gas generator 7 consisting of a burner 5 and a combustion chamber 6 in the lower central part. A cylindrical louver 1 is arranged so as to have a gap 8 in this cylindrical body 1.
0 and 11 are arranged in a double manner in the longitudinal direction, and the cylindrical louvers 10 and 11 are filled with granular materials 12 as objects to be preheated to form a granular material moving layer 13.
A particulate matter hopper 14 is connected to the upper end of the particulate matter moving layer 13 within the chamber. Further, at least between the particulate matter transfer layer 13 above the hot gas generator 7 and the particulate matter transfer layer 13 below the low temperature waste gas outlet 4.
and a slanted partition plate 15,1 between the cylindrical body 1 and the cylindrical body 1.
6 are arranged alternately. Although FIG. 1 shows a case where the partition plates are provided in two stages, it is also possible to provide three or more stages. The lower part of the cylindrical particulate matter moving layer 13 has a plurality of parts (in the drawing, as an example, there are four parts).
This bulging part 17 is connected to the granular preheated material outlet 3. 18 is a waste gas duct.
上記のように構成された本考案の粒状物の予熱
装置において、粒状物入口2から投入された熔成
燐肥原料、電気炉用原料、平炉用原料、その他の
粒塊状の鉱工業原料などは一定速度で二重の円筒
状ルーバ10,11内を移動し、この間、熱ガス
発生装置7から発生した熱ガスが矢印で示す方向
に粒状物移動層13内を複数回流れて粒状物を効
率よく予熱する。 In the granular material preheating device of the present invention configured as described above, the molten phosphorus fertilizer raw material, electric furnace raw material, open hearth raw material, and other granular mining and industrial raw materials inputted from the granular material inlet 2 are kept constant. During this time, the hot gas generated from the hot gas generator 7 flows through the particulate matter moving layer 13 multiple times in the direction shown by the arrow to efficiently move the particulates. Preheat.
本考案は上記のように構成されているので、つ
ぎのような効果を奏する。
Since the present invention is configured as described above, it has the following effects.
(1) 熱ガス発生装置と熱交換器とが一体化してい
るので、途中ダクトが無く放熱損失が少ない。
また装置全体をコンパクトにすることができ、
据付上有利である。(1) Since the hot gas generator and heat exchanger are integrated, there is no intermediate duct and there is little heat radiation loss.
In addition, the entire device can be made compact,
It is advantageous for installation.
(2) ユニツト化されているので、スケールアツプ
が容易となる。すなわち大容量への対応が容易
である。(2) Since it is unitized, it is easy to scale up. In other words, it is easy to handle large capacity.
(3) 粒状予熱物出口を複数個設けているので、被
予熱物の偏流が少なく、円滑に抜き出すことが
できる。(3) Since there are multiple outlets for the granular preheated material, there is less drifting of the preheated material and it can be smoothly extracted.
(4) 仕切板を傾斜した形状としているので、ルー
バからこぼれ出た被予熱物を粒状物移動層内に
自然に戻すことができる。(4) Since the partition plate has an inclined shape, the material to be preheated spilled from the louver can be naturally returned to the particulate matter movement layer.
第1図は本考案の粒状物の予熱装置の一実施例
を示す縦断面説明図、第2図は第1図におけるA
−A線断面図、第3図は第1図におけるB−B線
断面図である。
1……円筒状本体、2……粒状物入口、3……
粒状予熱物出口、4……低温廃ガス出口、5……
バーナ、6……燃焼室、7……熱ガス発生装置、
8……間隙、10,11……円筒状ルーバ、12
……粒状物、13……粒状物移動層、14……粒
状物ホツパ、15,16……傾斜した仕切板、1
7……膨出部、18……廃ガスダクト。
FIG. 1 is a vertical cross-sectional explanatory diagram showing an embodiment of the granular material preheating device of the present invention, and FIG.
- A sectional view, and FIG. 3 is a BB sectional view in FIG. 1. 1... Cylindrical main body, 2... Particulate matter inlet, 3...
Granular preheated material outlet, 4... Low temperature waste gas outlet, 5...
Burner, 6... Combustion chamber, 7... Hot gas generator,
8... Gap, 10, 11... Cylindrical louver, 12
... Granular material, 13... Granular material moving layer, 14... Granular material hopper, 15, 16... Slanted partition plate, 1
7...Bulging part, 18...Waste gas duct.
Claims (1)
出口3を有し、上側部に低温廃ガス出口4を有す
る円筒状本体1内に、間隙8を有するように円筒
状ルーバ10,11を縦方向に二重に配設し、円
筒状ルーバ間に被予熱物である粒状物12を充て
んして粒状物移動層13を形成し、円筒状本体1
内における粒状物移動層13の上端に粒状物ホツ
パ14を接続した粒状物移動層式の予熱装置にお
いて、円筒状本体1内の下部中央部に熱ガス発生
装置7を組み込み、熱ガス発生装置7の上側にお
ける粒状物移動層13,13の間、低温廃ガス出
口4の下側における粒状物移動層13と円筒状本
体1との間に傾斜した仕切板15,16を交互に
配置し、下端の粒状予熱物出口3を複数個配設し
たことを特徴とする粒状物の予熱装置。 Cylindrical louvers 10, 11 are provided with a gap 8 in a cylindrical body 1 having a granulate inlet 2 at the upper end, a granular preheat outlet 3 at the lower end, and a cold waste gas outlet 4 at the upper side. are arranged in a double manner in the longitudinal direction, and the cylindrical louvers are filled with granular materials 12, which are objects to be preheated, to form a granular material moving layer 13.
In a particulate matter moving bed type preheating device in which a particulate matter moving bed hopper 14 is connected to the upper end of a particulate matter moving bed 13 in a cylindrical body 1, a hot gas generating device 7 is incorporated in the lower central part of the cylindrical body 1. Slanted partition plates 15 and 16 are alternately arranged between the particulate matter transfer layers 13 and 13 on the upper side and between the particulate matter transfer layer 13 and the cylindrical body 1 below the low-temperature waste gas outlet 4. A granular material preheating device characterized in that a plurality of granular preheating material outlets 3 are provided.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP441784U JPS60117470U (en) | 1984-01-17 | 1984-01-17 | Granule preheating device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP441784U JPS60117470U (en) | 1984-01-17 | 1984-01-17 | Granule preheating device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60117470U JPS60117470U (en) | 1985-08-08 |
JPS643978Y2 true JPS643978Y2 (en) | 1989-02-02 |
Family
ID=30479965
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP441784U Granted JPS60117470U (en) | 1984-01-17 | 1984-01-17 | Granule preheating device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60117470U (en) |
-
1984
- 1984-01-17 JP JP441784U patent/JPS60117470U/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS60117470U (en) | 1985-08-08 |
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