JPH0420971B2 - - Google Patents
Info
- Publication number
- JPH0420971B2 JPH0420971B2 JP59227609A JP22760984A JPH0420971B2 JP H0420971 B2 JPH0420971 B2 JP H0420971B2 JP 59227609 A JP59227609 A JP 59227609A JP 22760984 A JP22760984 A JP 22760984A JP H0420971 B2 JPH0420971 B2 JP H0420971B2
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- rotor head
- rotor
- impeller
- pitch
- 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 - Lifetime
Links
- 239000007921 spray Substances 0.000 claims description 15
- 239000007788 liquid Substances 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 12
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 7
- 239000011701 zinc Substances 0.000 claims description 7
- 229910052725 zinc Inorganic materials 0.000 claims description 6
- 229910000978 Pb alloy Inorganic materials 0.000 claims description 2
- 229910001297 Zn alloy Inorganic materials 0.000 claims description 2
- 238000007654 immersion Methods 0.000 claims description 2
- 230000002093 peripheral effect Effects 0.000 claims description 2
- 230000003068 static effect Effects 0.000 claims description 2
- 229910052751 metal Inorganic materials 0.000 description 8
- 239000002184 metal Substances 0.000 description 8
- 239000007789 gas Substances 0.000 description 5
- 238000003723 Smelting Methods 0.000 description 4
- 229910045601 alloy Inorganic materials 0.000 description 3
- 239000000956 alloy Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 239000002956 ash Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Description
イ 産業上の利用分野
本発明は熱伝達又は物質移動の目的のために気
体中に液体を小滴として分散するための装置に関
する。それは精製又は凝縮の目的のために金属学
的溶融相、例えば溶融金属、合金、カワ又はカラ
ミを気相の中の小滴に分散するために特に適用で
きる。この分散された金属は、例えば溶融鉛が亜
鉛高炉製錬プロセスからの亜鉛蒸気の凝縮に使わ
れるように、凝縮媒体に使うことができる。
ロ 従来の技術
高炉での亜鉛の製錬はモルガンとウツヅによる
論文「亜鉛製錬への高炉の応用」(メタラルジカ
ル レビユー1971,16(156)11月、ページ161−
174)に一般的に記述されている。この論文のペ
ージ166の模式図からわかるように、炉軸の上部
は、下向きのダクトを経て、“鉛飛沫凝縮器”に
結合され、その凝縮器の中で炉ガスが、数段階に
わたつて、溶融鉛のプールの中に浸漬されたロー
タによつてつくられた溶融鉛の激しい噴霧をうけ
る。典型的な従来技術のロータヘツドは例えば
1972年2月9日発行の英国特許明細書1263165号
に示されている。
ハ 発明が解決しようとする問題点
本発明の目的は熱伝達又は物質移動の目的のた
めに気体中に液体を、小滴として、分散するため
の装置を提供することにある。
本発明の他の目的はこれまで達成されているよ
りも激しく、拘束され且つ急勾配の飛翔軌跡の液
滴噴霧を作ることにある。
ニ 問題を解決するための手段
本発明は、熱伝達又は物質移動の目的のために
気体中に液体を、小滴として、分散するための装
置であつて、ほゞ垂直の軸に取付けられ且つ少く
とも部分的にその液体中に浸漬されたロータヘツ
ドの回転によつて少くとも1つの液滴噴霧包絡面
が作られる装置に於いて、そのロータヘツドが
0.6と1.7の間のピツチ対直径比をもつ多翼らせん
形インペラの形をとることを特徴とする装置から
成る。
本発明によるロータヘツドは舶用プロペラの物
理的形状を基にしているが、翼形及び他の物理的
特性はこゝに述べた用途のために開発されてい
る。
この液体は金属学的溶融相、例えば溶融金属、
合金、カワ又はカラミであるのが好ましい。
この液体は金属蒸気を凝縮するために使われる
べき溶融金属又は合金であるのが好ましい。亜鉛
蒸気の場合はこの液体は溶融鉛/亜鉛合金であろ
う。
インペラは3枚羽根が好ましい。
このインペラのピツチ対直径比は0.6と1.3の間
であるのが好ましく、0.7と0.9の間が更に好まし
い。
インペラの外周先端速度は溶融鉛に対し8m/
秒乃至25m/秒の範囲内であるのが好ましく且つ
ロータの静的鉛表面以下への浸漬深さは100mmと
150mmの間であるのが好ましい。
種々の形のインペラ設計を試験したのが最良の
設計はピツチ対直径比が約0.75乃至0.85の3枚羽
根インペラであることがわかつた。典型的にその
ようなインペラは、従来技術のロータ平均初期飛
翔軌跡が水平に対し約30℃であるのに比べ、水平
に対し約50°乃至60°の平均初期飛翔軌跡の噴霧パ
ターンを生ずる。
ホ 発明の効果
本発明による装置によつて作られた噴霧パター
ンは噴霧密度が高く且つ噴霧パターン境界がはつ
きりしている。それでこの形式の装置によつて作
られた噴霧はコンパクトで飛翔軌跡が急勾配であ
る。
本発明によるロータヘツドの運転は、以下の数
値が示すように、従来のロータに比べて低い電力
消費でよいこともわかつた。
B. Field of Industrial Application The present invention relates to a device for dispersing liquid as droplets in a gas for the purpose of heat transfer or mass transfer. It is particularly applicable for dispersing metallurgical molten phases, such as molten metals, alloys, powders or ash, into droplets in a gas phase for purification or condensation purposes. This dispersed metal can be used as a condensing medium, for example, as molten lead is used to condense zinc vapor from a zinc blast furnace smelting process. B. Conventional technology The smelting of zinc in a blast furnace is based on the paper by Morgan and Utsuzu entitled "Application of Blast Furnace to Zinc Smelting", Metallurgical Review 1971, November 16 (156), page 161-
174). As can be seen from the schematic diagram on page 166 of this paper, the upper part of the furnace shaft is connected via a downward duct to a "lead splash condenser" in which the furnace gases are pumped in several stages. , subjected to a heavy spray of molten lead created by a rotor immersed in a pool of molten lead. A typical prior art rotor head is e.g.
It is shown in British Patent Specification No. 1263165, issued February 9, 1972. C. Problems to be Solved by the Invention It is an object of the present invention to provide an apparatus for dispersing a liquid in the form of droplets in a gas for the purpose of heat transfer or mass transfer. Another object of the present invention is to create a droplet spray with a more intense, constrained and steeper trajectory than hitherto achieved. D. Means for Solving the Problem The present invention is an apparatus for dispersing a liquid, as droplets, in a gas for the purpose of heat transfer or mass transfer, the device being mounted on a substantially vertical axis and In an apparatus in which at least one droplet spray envelope is created by rotation of a rotor head at least partially immersed in the liquid, the rotor head
It consists of a device characterized in that it takes the form of a multi-blade helical impeller with a pitch-to-diameter ratio between 0.6 and 1.7. The rotor head according to the present invention is based on the physical shape of a marine propeller, but the airfoil shape and other physical characteristics have been developed for the application described herein. This liquid is a metallurgical molten phase, e.g. molten metal,
Preferably, it is an alloy, a color, or a color. Preferably, this liquid is a molten metal or alloy that is to be used to condense metal vapors. In the case of zinc vapor, this liquid would be a molten lead/zinc alloy. The impeller preferably has three blades. Preferably, the pitch-to-diameter ratio of the impeller is between 0.6 and 1.3, more preferably between 0.7 and 0.9. The speed of the outer peripheral tip of the impeller is 8 m/m against molten lead.
The speed is preferably within the range of 25 m/s to 25 m/s, and the immersion depth below the static lead surface of the rotor is 100 mm.
Preferably it is between 150mm. Various impeller designs were tested and the best design was found to be a three blade impeller with a pitch to diameter ratio of about 0.75 to 0.85. Typically such impellers produce a spray pattern with an average initial trajectory of about 50° to 60° to the horizontal, compared to a prior art rotor average initial trajectory of about 30° to the horizontal. E. Effects of the Invention The spray pattern created by the apparatus according to the present invention has a high spray density and sharp boundaries of the spray pattern. The spray produced by this type of device is therefore compact and has a steep trajectory. It has also been found that operation of the rotor head according to the invention requires lower power consumption than conventional rotors, as shown by the following figures.
【表】
上の数値からロータを駆動する(有負荷から無
負荷まで)ために使われる有効電流は、従来のロ
ータに対し2.5乃至3.25A、本発明によるロータヘ
ツドに対し1.25乃至2.25Aの範囲にあることがわ
かる。
密度係数(溶融鉛/水)で拡大するとこれは鉛
中での有効電流が従来技術のロータに対し26乃至
34A、本発明によるロータヘツドに対し13乃至
24Aであることを表す。
ヘ 実施例と作用
添付の図面を参照して本発明を更に詳細に説明
する。
第1a図及び1b図に於いて、参照番号1は凝
縮器を示し、参照番号2はこの凝縮器と炉軸の間
の交叉ダクトを示し、そして参照番号3は炉軸へ
の入口を示す。
第1a図からわかるように本発明によるロータ
ヘツドにより生じた噴霧パターンは従来技術によ
るものよりよりコンパクトであり輪郭がはつきり
していると共に飛翔軌跡が急勾配であり、それで
噴霧が炉と凝縮器の初段との間の交叉ダクトの中
に達する傾向が少く、それで交叉ダクトの中の付
着物(レンガ構造物の冷却による)が減少し且つ
炉停止時間が減少する結果となる。
第2図は本発明による装置に使用するための典
型的な3枚羽根インペラを示す。
本発明による装置は金属蒸気の凝縮以外の目的
のために使われてもよい、例えばそれは金属噴霧
製錬に及び真空技術による溶融金属からの不純物
の除去に用途を見つけてもよい。[Table] From the above figures, the effective current used to drive the rotor (from loaded to unloaded) ranges from 2.5 to 3.25 A for a conventional rotor and from 1.25 to 2.25 A for a rotor head according to the invention. I understand that there is something. When magnified by the density factor (molten lead/water), this means that the effective current in lead is 26 to
34A, for the rotor head according to the invention from 13 to
Indicates that it is 24A. F. Examples and Effects The present invention will be described in further detail with reference to the accompanying drawings. In Figures 1a and 1b, reference numeral 1 designates the condenser, reference numeral 2 designates the cross-duct between this condenser and the furnace shaft, and reference numeral 3 designates the inlet to the furnace shaft. As can be seen from FIG. 1a, the spray pattern produced by the rotor head according to the invention is more compact and sharply contoured and has a steeper trajectory than that according to the prior art, so that the spray does not reach the furnace and condenser. less tendency to reach into the cross duct between the first stage and the first stage, resulting in less deposits in the cross duct (due to cooling of the brickwork) and reduced furnace shutdown time. FIG. 2 shows a typical three-blade impeller for use in a device according to the invention. The apparatus according to the invention may be used for purposes other than condensing metal vapors, for example it may find application in metal spray smelting and in the removal of impurities from molten metals by vacuum techniques.
第1a図は、鉛飛沫凝縮器の第1段階の断面に
重ねて、本発明によるロータヘツド(インペラ)
によつて作られた噴霧パターンの輪郭を示す。第
1b図は英国特許第1263165号の知見による、鉛
飛沫凝縮器に使用された従来技術のロータヘツド
により作られた噴霧パターンの輪郭を示す。第2
図は典型的なロータヘツドを示す。
1……凝縮器、2……交叉ダクト、3……炉軸
入口。
FIG. 1a shows a rotor head (impeller) according to the invention superimposed on a cross-section of the first stage of a lead droplet condenser.
The outline of the spray pattern created by is shown. Figure 1b shows the outline of the spray pattern produced by a prior art rotor head used in a lead droplet condenser, according to the findings of GB 1263165. Second
The figure shows a typical rotor head. 1...Condenser, 2...Cross duct, 3...Furnace shaft inlet.
Claims (1)
液体を、小滴として、分散するための装置であつ
て、ほゞ垂直の軸に取付けられ且つ少くとも部分
的にその液体中に浸漬されたロータヘツドの回転
によつて少くとも1つの液滴噴霧包絡面が作られ
る装置に於いて、そのロータヘツドが0.6と1.7の
間のピツチ対直径比をもつ多翼らせん形インペラ
の形をとることを特徴とする装置。 2 特許請求の範囲第1項記載の装置に於いて、
そのインペラが3枚の羽根を有し、ピツチ対直径
比が0.75乃至0.85であることを特徴とする装置。 3 熱伝達又は物質移動の目的のために気体中に
液体を、小滴として、分散する方法であつて、ほ
ぼ垂直の軸に取付けられ且つ少くとも部分的にそ
の液体中に浸漬されたロータヘツドの回転によつ
て少くとも1つの液滴噴霧包絡面が作られる方法
に於いて、そのロータヘツドが0.6と1.7の間のピ
ツチ対直径比をもつ多翼らせん形インペラの形を
とることを特徴とする方法。 4 特許請求の範囲第3項記載の方法に於いて、
その液体が亜鉛蒸気を凝縮するために使われる溶
融亜鉛/鉛合金である方法。 5 特許請求の範囲第4項記載の方法に於いて、
そのロータの外周先端速度が8m/秒乃至25m/
秒の範囲内にあり、ロータの静的鉛表面以下への
浸漬深さが100mmと150mmの間にあることを特徴と
する方法。 6 特許請求の範囲第3項から第5項のいずれか
1つに記載の方法に於いて、そのインペラが3枚
羽根を有し、ピツチ対直径比が0.75乃至0.85であ
ることを特徴とする方法。Claims: 1. Apparatus for dispersing a liquid, as droplets, in a gas for the purpose of heat transfer or mass transfer, the apparatus comprising: In an apparatus in which at least one droplet spray envelope is created by rotation of a rotor head immersed in the liquid, the rotor head is a multi-blade helical impeller having a pitch-to-diameter ratio between 0.6 and 1.7. A device characterized in that it takes the form of 2. In the device according to claim 1,
A device characterized in that the impeller has three blades and a pitch-to-diameter ratio of 0.75 to 0.85. 3. A method of dispersing a liquid, as droplets, in a gas for the purpose of heat transfer or mass transfer, the method comprising a rotor head mounted on a substantially vertical shaft and at least partially immersed in the liquid. A method in which at least one droplet spray envelope is created by rotation, characterized in that the rotor head takes the form of a multi-blade helical impeller with a pitch-to-diameter ratio between 0.6 and 1.7. Method. 4 In the method described in claim 3,
A method in which the liquid is a molten zinc/lead alloy used to condense zinc vapor. 5 In the method described in claim 4,
The outer peripheral tip speed of the rotor is 8m/sec to 25m/sec.
method, characterized in that the depth of immersion below the static lead surface of the rotor is between 100 mm and 150 mm. 6. The method according to any one of claims 3 to 5, characterized in that the impeller has three blades and a pitch-to-diameter ratio of 0.75 to 0.85. Method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59227609A JPS61110730A (en) | 1984-10-29 | 1984-10-29 | Apparatuas and method for dispersing liquid in gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59227609A JPS61110730A (en) | 1984-10-29 | 1984-10-29 | Apparatuas and method for dispersing liquid in gas |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61110730A JPS61110730A (en) | 1986-05-29 |
| JPH0420971B2 true JPH0420971B2 (en) | 1992-04-07 |
Family
ID=16863622
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59227609A Granted JPS61110730A (en) | 1984-10-29 | 1984-10-29 | Apparatuas and method for dispersing liquid in gas |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61110730A (en) |
-
1984
- 1984-10-29 JP JP59227609A patent/JPS61110730A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61110730A (en) | 1986-05-29 |
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