JPS6326345Y2 - - Google Patents
Info
- Publication number
- JPS6326345Y2 JPS6326345Y2 JP14187182U JP14187182U JPS6326345Y2 JP S6326345 Y2 JPS6326345 Y2 JP S6326345Y2 JP 14187182 U JP14187182 U JP 14187182U JP 14187182 U JP14187182 U JP 14187182U JP S6326345 Y2 JPS6326345 Y2 JP S6326345Y2
- Authority
- JP
- Japan
- Prior art keywords
- flow
- powder
- mixture
- distribution duct
- drifting
- 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
- 239000000203 mixture Substances 0.000 claims description 30
- 239000000843 powder Substances 0.000 claims description 27
- 238000011144 upstream manufacturing Methods 0.000 claims description 4
- 239000000463 material Substances 0.000 description 2
- 238000005452 bending Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
Description
【考案の詳細な説明】
本考案は、粉体及び気体混合物流通ダクト、更
に詳述すれば、流通ダクトの中に設置されて粉体
及び気体の混合物の略均等な濃度の流れを粉体の
濃度より大きい流れ部分と粉体の濃度の小さい流
れ部分とに分離したり、あるいはもともと粉体濃
度が不均一な混合物流れをその粉体濃度が均一化
となるようにする全く新規な偏流ブロツクに関す
るものである。[Detailed description of the invention] The present invention provides a powder and gas mixture distribution duct, more specifically, a powder and gas mixture distribution duct that is installed in the distribution duct to allow a powder and gas mixture to flow at a substantially uniform concentration. This invention relates to a completely new non-uniform flow block that separates a flow part with a higher concentration and a flow part with a lower powder concentration, or makes a mixture flow with an originally non-uniform powder concentration uniform. It is something.
以下図面を参照して本考案の実施例について詳
述する。 Embodiments of the present invention will be described in detail below with reference to the drawings.
第1図は本考案にしたがつて粉体及び気体混合
物流通ダクトの中に設置される偏流ブロツク自体
を示し、この偏流ブロツク1は粉体及び気体の混
合物の流れ2に対し縦長の断面を有して混合物流
れの方向に十分な厚さ(摩耗代)tを持つてい
る。したがつて、偏流ブロツク1は摩耗代を十分
にとることができるので、混合物流れ2中の粉体
により摩耗を受けながらも十分長時間使用するこ
とができ、また高価な耐摩耗材料で作る必要もな
い。 FIG. 1 shows the drifting block itself installed in a powder and gas mixture distribution duct according to the invention, this drifting block 1 having a longitudinally elongated cross section with respect to the flow 2 of the powder and gas mixture. It has a sufficient thickness (wear allowance) t in the direction of mixture flow. Therefore, the deflection block 1 has a sufficient wear allowance, so it can be used for a sufficiently long time even though it is worn by the powder in the mixture flow 2, and it does not need to be made of expensive wear-resistant materials. Nor.
第2図は第1図の偏流ブロツク1を粉体及び気
体混合物流通ダクト3の中に設置した一例を示
し、偏流ブロツク1は混合物流れ2の流路を上流
から下流に向つて片側(左側)にしだいに狭く限
定するように設置されている。したがつて、偏流
ブロツク1により流れを遮られた混合物流れ2は
矢印で示すように強制的に片側(左側)に導びか
れ、これにより流路4aの粉体濃度を流路4bよ
りも大きくすることができる。 FIG. 2 shows an example in which the biased flow block 1 shown in FIG. 1 is installed in the powder and gas mixture distribution duct 3. It is set up so that it gradually becomes narrower and more limited. Therefore, the mixture flow 2 whose flow is blocked by the deflection block 1 is forcibly guided to one side (left side) as shown by the arrow, thereby making the powder concentration in the flow path 4a higher than that in the flow path 4b. can do.
しかして、第1図に示した偏流ブロツク1を第
2図に示すように混合物流れ2中に設置しただけ
では、この偏流ブロツク1により流れを遮られた
混合物流れ2は必ずしも第2図に示されたように
流路の片側に完全に導びかれるわけではなく、第
3図に示すように偏流ブロツク1の面外へ流れる
ものを相当存在することになり、これでは本来の
目的を有効に達成できない。 However, if the deflection block 1 shown in FIG. 1 is simply installed in the mixture flow 2 as shown in FIG. The flow is not completely guided to one side of the flow path as shown in Figure 3, but there is a considerable amount of flow out of the plane of the deflection block 1, as shown in Figure 3. Unachievable.
そこで、本考案は、第4図に一例を示すよう
に、偏流ブロツク1の両側面に混合物流れ2の上
流へ延びるガイド5を設けてなる。このような一
対のガイド5を偏流ブロツク1の両側面に設ける
ことにより、混合物流れ2は第4図に矢印で示す
ように流れるので、混合物流れ2が偏流ブロツク
1の面外へ偏流するのを防止することができる。 Therefore, in the present invention, as an example shown in FIG. 4, guides 5 are provided on both sides of the deflection block 1 to extend upstream of the mixture flow 2. By providing such a pair of guides 5 on both sides of the deflection block 1, the mixture flow 2 flows as shown by the arrow in FIG. It can be prevented.
この場合、気体より密度の大きい粉体は慣性に
よりガイド5の上流で偏流する割合は気体より小
さい。したがつて、第4図において、ガイド5の
内側の混合物流れは粉体の濃度が高いが、ガイド
5の外側は粉体の濃度が低く、この粉体濃度の高
い混合物流れを偏流ブロツク1により第2図に示
した流路4aに導くことにより、この流路4aを
流れる混合物流れの粉体濃度が高められる。 In this case, the powder, which has a higher density than the gas, is drifted upstream of the guide 5 at a smaller rate than the gas due to inertia. Therefore, in FIG. 4, the mixture flow inside the guide 5 has a high concentration of powder, but the concentration of powder outside the guide 5 is low. By guiding the mixture to the flow path 4a shown in FIG. 2, the powder concentration of the mixture flow flowing through this flow path 4a is increased.
上述したように、第4図に示した如きガイドを
有する偏流ブロツクを使用することにより、粉体
及び気体の混合物の流れを粉体の濃度のより大き
い流れ部分と粉体の濃度の小さい流れ部分とに有
効に分離したり、あるいはもともと粉体濃度が不
均一な混合物流れを均一な粉体濃度にすることが
できる。 As mentioned above, by using a deflection block having a guide as shown in FIG. 4, the flow of a mixture of powder and gas can be divided into a flow part with a higher concentration of powder and a flow part with a lower concentration of powder. It is possible to effectively separate the powders from each other, or to make a mixture flow, which originally has a non-uniform powder concentration, to a uniform powder concentration.
また、この偏流ブロツクは、前述したように、
混合物流れに対し縦長の断面を有しているので、
摩耗に対して十分摩耗代をとることができ、した
がつて長時間の使用に耐えることができ、特に摩
耗性の高い粉体に対して有効ある。更に、高価な
耐摩耗性材料で偏流ブロツクを作る必要もなく、
しかも構造が簡単であるとともに、混合物流れの
流路を曲げることなく偏流ブロツクを設置するこ
とができるなどの利点もある。 In addition, as mentioned above, this drift block
Since it has a longitudinal cross section with respect to the mixture flow,
It can provide a sufficient amount of wear allowance against wear and can therefore withstand long-term use, and is particularly effective against highly abrasive powders. Furthermore, there is no need to create drift blocks using expensive wear-resistant materials.
Moreover, it has the advantage that it has a simple structure and that a deflection block can be installed without bending the flow path of the mixture flow.
第5図は本考案にしたがつて多数の偏流ブロツ
ク1を粉体及び気体混合物流通ダクト3の中にそ
のダクト巾方向に間隔を置いて並列に設置した一
例を示し、両側の偏流ブロツク1は一方の側面に
のみガイド5を有している。しかして、第5図
中、偏流ブロツク1の幅寸法aとブロツク間の寸
法bとの割合を変えることにより、またガイド5
のブロツクからの突出寸法cの割合を変えること
により、偏流効果を変えることができる。 FIG. 5 shows an example in which a large number of drifting blocks 1 are installed in parallel in a powder and gas mixture distribution duct 3 at intervals in the width direction of the duct according to the present invention, and the drifting blocks 1 on both sides are It has a guide 5 only on one side. Therefore, in FIG. 5, by changing the ratio of the width dimension a of the drifting block 1 to the dimension b between the blocks, the guide 5
By changing the ratio of the protruding dimension c from the block, the drifting effect can be changed.
第6図は同様に多数の偏流ブロツク1を四角形
断面の流通ダクト13の中に一段にして設置した
一例を示す。 FIG. 6 similarly shows an example in which a large number of drifting blocks 1 are installed in one stage in a distribution duct 13 having a rectangular cross section.
第7図は多数の偏流ブロツク1を二段にして四
角形断面の流通ダクト13の中に設置した一例を
示し、各段の多数の偏流ブロツク1は混合物流れ
2に対して交互に配置されている。 FIG. 7 shows an example in which a large number of drifting blocks 1 are installed in two stages in a distribution duct 13 with a rectangular cross section, and the large number of drifting blocks 1 in each stage are arranged alternately with respect to the mixture flow 2. .
第8図は、多数の偏流ブロツク1を円形断面の
流通ダクト23の中に設置した二例を示す。 FIG. 8 shows two examples in which a large number of drifting blocks 1 are installed in a circulation duct 23 having a circular cross section.
第1図は本考案による粉体及び気体混合物流通
ダクトの中に設置される偏流ブロツク自体を示す
斜視図、第2図及び第3図は第1図に示した偏流
ブロツク体自体の作用を示す側面図及び正面図、
第4図は両側面にガイドを有する偏流ブロツクの
作用を示す正面図、第5図は本考案にしたがつて
多数の偏流ブロツクを粉体及び気体混合物流通ダ
クトの中にそのダクト巾方向に間隔を置いて並列
に設置した一例を示す正面図、第6図は多数の偏
流ダクトを四角形断面の流通ダクトの中に一段に
して設置した一例を示し、aは正面図、bはaの
B−B線に沿う側面断面図、cはbのC−C線に
沿う底面図、第7図は多数の偏流ダクトを四角形
断面の流通ダクトの中に二段にして設置した一例
を示し、aは正面図、bはaのB−B線に沿う側
面断面図、cはbのC−C線に沿う底面図、dは
bのD−D線に沿う底面図、第8図のa及びbは
多数の偏流ブロツクを円形断面の流通ダクトの中
に設置した二例を該ダクトの直角断面に沿つて示
す底面図である。
1……偏流ブロツク、2……粉体及び気体混合
物の流れ、5……ガイド。
Fig. 1 is a perspective view showing the deflection block itself installed in a powder and gas mixture distribution duct according to the present invention, and Figs. 2 and 3 show the action of the deflection block itself shown in Fig. 1. side view and front view,
Fig. 4 is a front view showing the action of a deflection block having guides on both sides, and Fig. 5 shows a large number of deflection blocks according to the present invention placed in a powder and gas mixture distribution duct at intervals in the width direction of the duct. Fig. 6 shows an example in which a large number of drifting ducts are installed in a single stage in a distribution duct with a rectangular cross section, a is a front view, and b is a B- of a. Fig. 7 shows an example in which a large number of drifting ducts are installed in two stages in a distribution duct with a rectangular cross section; Front view, b is a side sectional view taken along line B-B of a, c is a bottom view taken along line C-C of b, d is a bottom view taken along line D-D of b, a and b in Figure 8. These are bottom views showing two examples in which a large number of drifting blocks are installed in a circulation duct having a circular cross section, taken along a right-angled cross section of the duct. 1...Difference flow block, 2...Flow of powder and gas mixture, 5...Guide.
Claims (1)
れの流路を上流から下流に向つて片側にしだいに
狭く限定する偏流ブロツクを流通ダクトの巾方向
に間隔を置いて多数並列に設置し、これらの各偏
流ブロツクは、混合物流れに対し縦長の断面を有
するとともに、その両側面に混合物流れの上流へ
延びる一対のガイドを有してなることを特徴とす
る粉対及び気体混合物流通ダクト。 During the flow of a mixture of powder and gas, a large number of deflection blocks are installed in parallel at intervals in the width direction of the distribution duct to narrow the flow path of the mixture flow from upstream to downstream. A powder and gas mixture distribution duct characterized in that each deflection block has a vertically elongated cross section with respect to the mixture flow, and has a pair of guides on both sides thereof extending upstream of the mixture flow.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14187182U JPS5948737U (en) | 1982-09-21 | 1982-09-21 | Powder and gas mixture distribution duct |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14187182U JPS5948737U (en) | 1982-09-21 | 1982-09-21 | Powder and gas mixture distribution duct |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5948737U JPS5948737U (en) | 1984-03-31 |
JPS6326345Y2 true JPS6326345Y2 (en) | 1988-07-18 |
Family
ID=30317172
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14187182U Granted JPS5948737U (en) | 1982-09-21 | 1982-09-21 | Powder and gas mixture distribution duct |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5948737U (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CH669336A5 (en) * | 1985-12-11 | 1989-03-15 | Sulzer Ag |
-
1982
- 1982-09-21 JP JP14187182U patent/JPS5948737U/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS5948737U (en) | 1984-03-31 |
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