JPS6145495B2 - - Google Patents
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- Publication number
- JPS6145495B2 JPS6145495B2 JP1944579A JP1944579A JPS6145495B2 JP S6145495 B2 JPS6145495 B2 JP S6145495B2 JP 1944579 A JP1944579 A JP 1944579A JP 1944579 A JP1944579 A JP 1944579A JP S6145495 B2 JPS6145495 B2 JP S6145495B2
- Authority
- JP
- Japan
- Prior art keywords
- combustion
- gas
- cavity
- combustion chamber
- premixing
- 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
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Description
この発明は火炎溶射に用いる粉体溶射用バーナ
ーノズルに関する。
従来の粉体溶射装置では燃料ガスとして
O3H6,C4H10等のガスを用いた場合に充分に高い
火炎温度が得られず、セラミツクたとえばA
2O3のような高融点の粉体原料を火炎溶射するこ
とができなかつた。そこで、高融点の粉体原料を
火炎溶射する場合には、一般に燃料ガスとして
O2H2を用いていた。しかし、O2H2は自己分解を
起す性質を有するため供給圧力を低く保つ必要が
あり、大容量処理には不向きである。
この発明はこのような事情を考慮してなされた
ものであり、その目的は燃料ガスとしてO2H8,
O4H10等を用いても充分に高い火炎温度を得るこ
とができ、セラミツク等高融点の粉体材料を火炎
溶射できる粉体溶射用のバーナーノズルを供給す
ることにある。さらに、この発明の他の目的は粉
体原料を高い溶着率で火炎溶射できるバーナーノ
ズルを供給することにある。
以下、この発明の一実施例について説明する。
第1図、第2図および第3図はこの施例に係るバ
ーナーノズル本体9を示している。第1図、第2
図および第3図において、銅製の内筒10にはこ
れを囲むように円筒状の外筒11が固定して取り
付けられている。内筒10には円柱状の空洞12
と、円錐台形状の空洞13と、この空洞12に比
較して径の小さい円柱状の空洞からなる気固流供
給孔14とが形成されている。これら空洞12,
13は予混合・燃焼室15を構成し、この予混
合・燃焼室15の空洞12側の端部が火炎噴出口
15aとして開口されている。予混合・燃焼室1
5の他方の空洞13側の端部は前述の気固流供給
孔14につながつている。こうして、気固流(粉
体原料、たとえばA2O3をC3H8,C4,H10等の
燃料ガスたとえばO3H8で輸送する流れ。以下、
同様)が、気固流供給孔14を介して予混合・燃
焼室15に導入され、そののち火炎とされて火炎
噴出口15aから噴射されるのである。
また、内筒10の予混合・燃焼室15側の外径
に外筒11の内径と一致しており、この予混合・
燃焼室15側において、内筒10の外周面と外筒
11の内周面とが密着している。他方、内筒10
の気固流供給孔14側の外径は外筒11の内径よ
り小さくなつており、この気固流供給孔14側に
おいて、内筒10の外周面と外筒11の内周面と
の間に環状の空隙が形成され、この空隙が支燃ガ
ス案内孔16を構成している。
予混合・燃焼室15の空洞13の壁面(錐面)
には母線方向の異なる2つの位置ごとに4個づつ
(本実施例には4個づつ、一般には4個に限らず
複数個)の小径の第1支燃ガス供給孔17a,
…,17b,…がそれぞれ環状の配列で設けられ
ている。これらの供給孔17a,17b,…,は
前述の支燃ガス案内孔16から前述の予混合・燃
焼室15までその予混合・燃焼室15の空洞の壁
面(錐面)の接線方向に穿ち設けられている。さ
らに、予混合・燃焼室15の空洞13の壁面(錐
面)には前述の母線方向の異なる2つの位置より
も空洞12側の位置に、8個の第2支燃ガス供給
孔17c,…が環状の配列で設けられている。こ
の第2支燃ガス供給孔17c,…は予混合・燃焼
室15の火炎噴出口15a方向でかつ予混合・燃
焼室15の軸線上に収れんするように、支燃ガス
案内孔16側から予混合・燃焼室15側まで穿ち
設けられている。
こうして、酸素ガスまたは酸素富化空気(以
下、支燃ガスとする)が支燃ガス案内孔16およ
び支燃ガス供給孔17a,…,17b,…17
c,…を経て予混合・燃焼室15に供給され、前
述の気固流と混合される。
つぎに、このように構成された粉体溶射用バー
ナーノズルの機能について説明する。第1図、第
2図および第3図において、粉体原料A2O3は
燃料ガスC3H8に輸送されて気固流として約20
m/secの流速で矢印aで示すように気固流供給
孔14内を案内され、さらに予混合・燃焼室15
に噴出される。また支燃ガスは支燃ガス案内孔1
6内を約20の/secの流速で矢印bで示すように
導入され、そののち支燃ガス供給孔17a,…,
17b,…17c,…を経て約150m/secの流速
でそれぞれ矢印c,d,eで示すように予混合・
燃焼室15に噴出される。その結果、燃料ガスお
よび支燃ガスが混合される。
すなわち、支燃ガス供給孔17a,…,17
b,…,17c,…はそれぞれ母線方向の異なる
位置に設けられているため、前述の気固流はまず
供給孔17a,…の近くを通過し、そののち順次
供給孔17b,…17c,…のそれぞれの近くを
通過していく。その結果、この気固流にはまず供
給孔17a,…から噴出された支燃ガスが混合さ
れ、そののち供給孔17b,…17c,…からそ
れぞれ噴出された支燃ガスが順次、混合される。
この際、第1支燃ガス供給孔17a,…17b,
…は予混合・燃焼室15の空洞13の錐面の接線
方向に向いており、また、第2支燃ガス供給孔1
7c,…は火炎噴出口15a方向でかつ予混合・
燃焼室15の軸線上に収れんするようになつてい
るため、前述の支燃ガスの噴出によつて、気固流
供給孔14からの気固流のスムーズな供給が妨げ
られる流れが乱れることがない。
こうして、気固流がスムーズに供給され、その
うえ、この気固流に支燃ガスが完全に混合され
る。したがつて、予混合・燃焼室15からの火炎
噴出口15aの外側の領域にわたつて高い火炎温
度ゾーンが形成され、気固流中の粉体原料が高融
点のものであつても、火炎噴出口15aの外側の
領域までに完全に溶融される。火炎噴出口15a
から噴出されるガス(火炎)の流速はほぼ250
m/secであり、大部分が溶融された粉体原料の
流速(速度)はほぼ150m/secである。粉体原料
はこの流速で火炎噴出口15aを噴出し、火炎中
で完全に溶融した後母材(図示しない)に溶着す
る。
また、第1支燃ガス供給孔17a,…は予混
合・燃焼室15の錐面に環状の配列で、しかもこ
の錐面の接線方向に向いて設けられている。同様
に、第1支燃ガス供給孔17b,…も予混合燃焼
室15に設けられている。さらに、第2支燃ガス
供給孔17c,…は予混合・燃焼室15の錐面に
環状の配列で、しかも火炎噴出口15aの方向で
かつ予混合・燃焼室15の軸線上で収れんするよ
うに設けられている。
したがつて、気固流中の粉体原料をむだに飛散
させずにすみ、気固流中の粉体原料を前述した火
炎の中心(予混合・燃焼室15の中心軸方向)に
集中させることができ、そのため高溶着率の溶射
を実現できる。上記ノズルを用いた溶射実験によ
れば、「表」に示すように、燃料ガスおよび粉体
原料としてそれぞれO3H8およびA2O3(純粋)
を採用した場合でも極めて高い溶着率で溶射が行
えた。
The present invention relates to a burner nozzle for powder thermal spraying used in flame thermal spraying. In conventional powder spray equipment, it is used as fuel gas.
When using gases such as O 3 H 6 and C 4 H 10 , a sufficiently high flame temperature cannot be obtained, and ceramics such as A
It was not possible to flame spray a powder material with a high melting point such as 2 O 3 . Therefore, when flame spraying a powder raw material with a high melting point, it is generally used as a fuel gas.
O2H2 was used . However, since O 2 H 2 has the property of causing self-decomposition, it is necessary to keep the supply pressure low, making it unsuitable for large-capacity processing. This invention was made in consideration of these circumstances, and its purpose is to use O 2 H 8 ,
The object of the present invention is to provide a burner nozzle for powder thermal spraying that can obtain a sufficiently high flame temperature even when using O 4 H 10 or the like and can flame spray powder materials with a high melting point such as ceramics. Furthermore, another object of the present invention is to provide a burner nozzle capable of flame spraying powder raw materials at a high welding rate. An embodiment of the present invention will be described below.
1, 2 and 3 show a burner nozzle body 9 according to this embodiment. Figures 1 and 2
In the figures and FIG. 3, a cylindrical outer cylinder 11 is fixedly attached to an inner cylinder 10 made of copper so as to surround it. The inner cylinder 10 has a cylindrical cavity 12.
A truncated cone-shaped cavity 13 and a gas-solid flow supply hole 14 formed of a cylindrical cavity having a smaller diameter than the cavity 12 are formed. These cavities 12,
Reference numeral 13 constitutes a premixing/combustion chamber 15, and the end of the premixing/combustion chamber 15 on the cavity 12 side is opened as a flame jet port 15a. Premixing/combustion chamber 1
The end of 5 on the other cavity 13 side is connected to the gas-solid flow supply hole 14 described above. In this way, a gas-solid flow (a flow in which powder raw material, e.g. A 2 O 3 is transported with a fuel gas such as C 3 H 8 , C 4 , H 10 etc., e.g. O 3 H 8 ; hereinafter,
(similar) is introduced into the premixing/combustion chamber 15 through the gas-solid flow supply hole 14, and is then turned into a flame and injected from the flame jet port 15a. In addition, the outer diameter of the inner cylinder 10 on the premixing/combustion chamber 15 side matches the inner diameter of the outer cylinder 11, and this premixing/combustion chamber 15 side matches the inner diameter of the outer cylinder 11.
On the combustion chamber 15 side, the outer peripheral surface of the inner cylinder 10 and the inner peripheral surface of the outer cylinder 11 are in close contact with each other. On the other hand, the inner cylinder 10
The outer diameter of the gas-solid flow supply hole 14 side is smaller than the inner diameter of the outer cylinder 11, and on the gas-solid flow supply hole 14 side, there is a gap between the outer peripheral surface of the inner cylinder 10 and the inner peripheral surface of the outer cylinder 11. An annular gap is formed in the opening, and this gap constitutes the combustion-supporting gas guide hole 16. Wall surface (conical surface) of cavity 13 of premixing/combustion chamber 15
are provided with four small diameter first combustion-supporting gas supply holes 17a (four in this embodiment, generally not limited to four but plural) at two different positions in the generatrix direction.
..., 17b, ... are provided in a circular arrangement. These supply holes 17a, 17b, . . . are bored in the tangential direction of the wall surface (conical surface) of the cavity of the premixing/combustion chamber 15 from the combustion-supporting gas guide hole 16 to the premixing/combustion chamber 15. It is being Further, on the wall surface (conical surface) of the cavity 13 of the premixing/combustion chamber 15, eight second combustion-supporting gas supply holes 17c, . are arranged in a circular arrangement. The second combustion-supporting gas supply holes 17c, . It is perforated up to the mixing/combustion chamber 15 side. In this way, oxygen gas or oxygen-enriched air (hereinafter referred to as combustion-supporting gas) is supplied to the combustion-supporting gas guide hole 16 and the combustion-supporting gas supply hole 17a, ..., 17b, ...17.
It is supplied to the premixing/combustion chamber 15 via c, . . . and mixed with the aforementioned gas-solid stream. Next, the function of the burner nozzle for powder thermal spraying configured as described above will be explained. In Figures 1, 2, and 3, powder raw material A 2 O 3 is transported to fuel gas C 3 H 8 as a gas-solid stream of about 20
The gas-solid flow is guided through the gas-solid flow supply hole 14 as shown by the arrow a at a flow rate of m/sec, and further flows into the premixing/combustion chamber 15.
It is squirted. In addition, the combustion-supporting gas is connected to the combustion-supporting gas guide hole 1.
6 at a flow rate of about 20/sec as shown by the arrow b, and then the combustion-supporting gas supply holes 17a,...,
17b, ... 17c, ... at a flow rate of approximately 150 m/sec as shown by arrows c, d, and e, respectively.
It is ejected into the combustion chamber 15. As a result, the fuel gas and combustion supporting gas are mixed. That is, the combustion supporting gas supply holes 17a,...,17
Since b,..., 17c,... are provided at different positions in the generatrix direction, the gas-solid flow described above first passes near the supply holes 17a,..., and then sequentially passes through the supply holes 17b,..., 17c,... passing near each of them. As a result, the combustion-supporting gases ejected from the supply holes 17a, . .
At this time, the first combustion supporting gas supply holes 17a,...17b,
... is oriented in the tangential direction of the conical surface of the cavity 13 of the premixing/combustion chamber 15, and the second combustion supporting gas supply hole 1
7c, ... are in the direction of the flame outlet 15a and are premixed and
Since the gas is converged on the axis of the combustion chamber 15, the above-mentioned jetting of the combustion-supporting gas does not cause disturbances in the flow that prevent the smooth supply of the gas-solid flow from the gas-solid flow supply hole 14. do not have. In this way, the gas-solid flow is smoothly supplied, and moreover, the combustion supporting gas is completely mixed with the gas-solid flow. Therefore, a high flame temperature zone is formed over the area outside the flame jet port 15a from the premixing/combustion chamber 15, and even if the powder raw material in the gas-solid flow has a high melting point, the flame It is completely melted up to the area outside the spout 15a. Flame spout 15a
The flow velocity of the gas (flame) ejected from is approximately 250
m/sec, and the flow rate (velocity) of the mostly molten powder raw material is approximately 150 m/sec. The powder raw material is ejected from the flame outlet 15a at this flow rate, completely melted in the flame, and then welded to the base material (not shown). Further, the first combustion-supporting gas supply holes 17a, . . . are arranged in an annular arrangement on the conical surface of the premixing/combustion chamber 15, and are oriented in the tangential direction of this conical surface. Similarly, the first combustion supporting gas supply holes 17b, . . . are also provided in the premix combustion chamber 15. Further, the second combustion-supporting gas supply holes 17c, ... are arranged in an annular manner on the conical surface of the premixing/combustion chamber 15, and converge in the direction of the flame jet port 15a and on the axis of the premixing/combustion chamber 15. It is set in. Therefore, the powder raw material in the gas-solid flow is not needlessly scattered, and the powder raw material in the gas-solid flow is concentrated at the center of the flame (in the direction of the central axis of the premixing/combustion chamber 15). Therefore, thermal spraying with a high welding rate can be achieved. According to thermal spraying experiments using the above nozzle, as shown in the table, O 3 H 8 and A 2 O 3 (pure) were used as fuel gas and powder raw material, respectively.
Even when using this method, thermal spraying was possible with an extremely high welding rate.
【表】
なお、この実施例では気固流として粉体原料を
燃料ガスで輸送させたものを用いたが、燃料ガス
と支燃ガスとの混合ガスで粉体原料を輸送させて
もよい。また、第2支燃ガス供給孔17cを環状
の配列で設けられた小径の孔としたが、環状のス
リツトによつて構成するようにしてもよい。更に
この第2支燃ガス供給孔は前記予混合・燃焼室の
前後方向に複数段設けても良い。
以上、実施例について説明したように、この発
明によれば、気固流に支燃ガスを完全に混合で
き、その結果、高い火炎温度を実現でき、しかも
気固流中の粉体原料を火炎の中心に集めることが
できるため、燃料ガスとしてC3H8,C4H10等を用
いても高融点の粉体原料を高い溶着率で溶射する
ことができる。[Table] In this example, the powder raw material was transported using fuel gas as a gas-solid flow, but the powder raw material may be transported using a mixed gas of fuel gas and combustion supporting gas. Furthermore, although the second combustion-supporting gas supply holes 17c are small diameter holes arranged in an annular arrangement, they may be formed by annular slits. Furthermore, the second combustion-supporting gas supply holes may be provided in multiple stages in the longitudinal direction of the premixing/combustion chamber. As described above with respect to the embodiments, according to the present invention, it is possible to completely mix the combustion-supporting gas into the gas-solid flow, and as a result, it is possible to achieve a high flame temperature, and moreover, the powder raw material in the gas-solid flow can be mixed with the flame. Since it can be collected at the center of the fuel gas, powder raw materials with high melting points can be thermally sprayed with a high welding rate even if C 3 H 8 , C 4 H 10 , etc. are used as the fuel gas.
図面はこの発明の一実施例を示すもので、第1
図は縦断面図、第2図は第1図の−線に沿つ
て断面する横断面図、第3図は第1図の−線
に沿つて断面する横断面図である。
10…内筒、11…外筒、14…気固流供給
孔、15…予混合・燃焼室、15a…火炎噴出
口、16…支燃ガス案内孔、17a,17b,…
第1支燃ガス供給孔、17c…第2支燃ガス供給
孔。
The drawings show one embodiment of the invention.
2 is a cross-sectional view taken along the - line in FIG. 1, and FIG. 3 is a cross-sectional view taken along the - line in FIG. 1. DESCRIPTION OF SYMBOLS 10... Inner cylinder, 11... Outer cylinder, 14... Gas-solid flow supply hole, 15... Premixing/combustion chamber, 15a... Flame jet port, 16... Combustion supporting gas guide hole, 17a, 17b,...
First combustion-supporting gas supply hole, 17c...second combustion-supporting gas supply hole.
Claims (1)
円形で該火炎噴出口方向に向けて拡開する空洞よ
りなる予混合・燃焼室を有し、前記空洞の後端部
に該空洞内に向けて気固流を噴出する気固流供給
孔が連設され、前記空洞の軸線を中心として環状
に配置され、かつ前記円形の横断面の接線方向に
向くように前記予混合・燃焼室に連通する複数の
第1支燃ガス供給孔を一段または前記空洞の前後
方向に複数段形成し、前記空洞の軸線を中心とし
て環状に配置され、かつ前記火炎噴出口に向けて
前記軸線に漸次近づくような方向を有して穿孔ま
たは配置された小孔群またはスリツトを穿設して
なる第2支燃ガス供給孔を一段または前記空洞の
前後方向に複数段形成したことを特徴とする粉体
溶射用バーナーノズル。1. A premixing/combustion chamber having a front end opening as a flame outlet, a circular cross section and a cavity that expands toward the flame outlet, and a rear end of the cavity having a gas-solid flow supply holes for ejecting a gas-solid flow towards the premixing/combustion chamber, arranged in a ring shape around the axis of the cavity, and oriented in the tangential direction of the circular cross section; A plurality of communicating first combustion-supporting gas supply holes are formed in one stage or in a plurality of stages in the front-rear direction of the cavity, are arranged in an annular shape around the axis of the cavity, and gradually approach the axis toward the flame jet port. A powder characterized by forming one stage or a plurality of stages of second combustion-supporting gas supply holes in the front-rear direction of the cavity, which are formed by drilling or slits or groups of small holes drilled or arranged in such a direction. Burner nozzle for thermal spraying.
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1944579A JPS55111860A (en) | 1979-02-21 | 1979-02-21 | Burner nozzle for flame-spraying pulverized material |
| DE19803006558 DE3006558A1 (en) | 1979-02-21 | 1980-02-21 | POWDER SPRAY COATING BURNER |
| FR8004126A FR2449479A1 (en) | 1979-02-21 | 1980-02-21 | BURNER FOR POWDER SPRAY COATING |
| US06/595,344 US4569479A (en) | 1979-02-21 | 1984-03-30 | Burner for powder spray coating |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1944579A JPS55111860A (en) | 1979-02-21 | 1979-02-21 | Burner nozzle for flame-spraying pulverized material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS55111860A JPS55111860A (en) | 1980-08-28 |
| JPS6145495B2 true JPS6145495B2 (en) | 1986-10-08 |
Family
ID=11999498
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1944579A Granted JPS55111860A (en) | 1979-02-21 | 1979-02-21 | Burner nozzle for flame-spraying pulverized material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS55111860A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62102082A (en) * | 1985-10-28 | 1987-05-12 | 川崎製鉄株式会社 | Flame spraying repair method and device thereof |
| JP2007010173A (en) * | 2005-06-28 | 2007-01-18 | Tama Tlo Kk | Nozzle burner device and thermal spraying device |
| KR100924821B1 (en) | 2009-06-16 | 2009-11-03 | 주식회사 봉화라이너 | Spray coating apparatus |
-
1979
- 1979-02-21 JP JP1944579A patent/JPS55111860A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS55111860A (en) | 1980-08-28 |
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