Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS6135466B2 - - Google Patents
[go: Go Back, main page]

JPS6135466B2 - - Google Patents

Info

Publication number
JPS6135466B2
JPS6135466B2 JP14334282A JP14334282A JPS6135466B2 JP S6135466 B2 JPS6135466 B2 JP S6135466B2 JP 14334282 A JP14334282 A JP 14334282A JP 14334282 A JP14334282 A JP 14334282A JP S6135466 B2 JPS6135466 B2 JP S6135466B2
Authority
JP
Japan
Prior art keywords
nozzle
refractory
powder
combustion
oxygen
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
Application number
JP14334282A
Other languages
Japanese (ja)
Other versions
JPS5935775A (en
Inventor
Hiroyuki Ishimatsu
Norio Kotabe
Kazuo Hamai
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP14334282A priority Critical patent/JPS5935775A/en
Publication of JPS5935775A publication Critical patent/JPS5935775A/en
Publication of JPS6135466B2 publication Critical patent/JPS6135466B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Furnace Housings, Linings, Walls, And Ceilings (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は耐火物内張築造物の補修方法に関する
ものである。 高温炉に供される耐火物内張り築造物は、使用
中に熱的あるいは化学的雰囲気により劣化・脆化
し、損耗される。このためこうして耐火物内張り
築造物は一般に局部的な中間補修により、寿命の
延長が図られている。 通常、これら耐火物内張り築造物の中間補修は
粉末耐火物を水で混練した不定形耐火物を流し込
んで成形するか、或いは、これを被補修面に吹き
付ける方法により行なわれているが、常温で作業
を行なうためには、高温築造物の降温と昇温によ
る耐火物の熱的スポーリングが不可避であり、補
修施工部の強度が弱い。また、これを熱間で行な
おうとすれば高温部の被補修面に施工するため、
付着性が悪く、水分蒸発のために気孔率が高く、
耐火度が不良である。 また、近年、新しい耐火物の補修方法として、
耐火物粉末の溶射補修方法が一部の耐火物築造物
に採用されつつあるが、これまでの粉末溶射法は
主に気体燃料を使用する方法と固体燃料を使用す
る方法によつて行なわれていた。気体燃料を使用
する粉末溶射法においては、LNG,LPG,アセ
チレンなどの分子量の低い炭化水素化合物を燃料
として使用するため一般に火炎温度が低くMgO
系などの高融点の耐火物を溶融できないため、適
用範囲が限られており、また実用化された設備も
500Kg/H程度の比較的小容量であるため適用範
囲が限られていた。また、気体燃料と酸素などの
支燃剤混合気の異常燃焼に伴なう危険性を孕んで
いた。 一方、石炭、コークス粉など固体燃料を使用す
る溶射法においては、燃焼反応に要する反応時間
が長いため、低温度の長火炎を形成し、MgO系
の高融点材料を溶融できない。加えて、石灰、コ
ークス粉などの燃料中に存在する灰分(SiO2
Fe2O3,Al2O3など)による汚染、即ち、耐火度
〓〓〓〓
の低下という欠点を有していた。 上述のように、従来の耐火物内張り築造物の補
修方法は不定形耐火物の湿式補修においては、本
質的に耐火度が低く、また従来方式の溶射補修方
法においては、高融点材料を溶融できないため、
低気孔・高密度・高融点・高耐火性を有する施工
体を形成できず、耐蝕性において湿式法には勝る
ものの、未だ補修頻度が多く、適用の範囲が小さ
いなどの欠点があつた。 本発明は上記のような従来の溶射法の欠点を改
善し、低気孔、高密度、高融点、高耐火性を有す
る耐火物補修面を形成する耐火物内張り築造物の
補修方法に関するものである。 本発明は耐火物内張り築造物の補修において、
液体燃料を管内ゲージ圧力1Kg/cm2−G(以下単
に1Kg/cm2と称する)以上の噴霧圧力によりノズ
ルより噴霧し、噴霧された液体燃料の支燃剤とし
て酸素を200m/s以上の流速でノズルより吐出
させて燃焼させた火炎中に、酸素により搬送され
た耐火物粉末を10m/s以上90m/s以下の搬送
気体速度でノズルより供給する三種流体のノズル
孔を有する粉末溶射器を使用して補修することに
より、低気孔、高密度、高融点、高耐火性を有す
る耐火物補修面を形成するものである。 以下、本発明の一実施例を図について説明す
る。 第1図は本発明の一実施例による粉末溶射装置
である。図において、1は酸素などの支燃剤のノ
ズルであり、2は粉末噴射ノズルで、酸素や空気
により搬送された耐火物粉末を吐出するものであ
る。3は、液体燃料の噴射ノズルで、噴霧された
液滴径を小さくするため、粉末は5の分配器によ
り各ノズルに配分される先端において旋回翼を内
包し、かつ先端を絞つたノズルが用いられる。4
は冷却筒であり、冷却水の流路が内包されてい
る。 粉末溶射器において耐火物粉末を火炎中で溶融
し、耐火物内張に付着するためには、耐火物粉末
の融点以上に火炎温度を高める必要がある。とこ
ろで、液体燃料の燃焼状況、即ち火炎の性状は霧
化された燃料の液滴の状況と液滴と支燃剤の混合
状況によつて決定され火炎温度を高めるために
は、燃料液滴の径を小さくして、支燃剤との接触
面積を大きくするとともに、燃料と支燃剤の混合
を良好にせねばならない。 そのため、高融点耐火物粉末を溶射するには、
液体燃料系溶射器において、液体燃料の霧化液滴
径を小さくし、かつ燃料と支燃剤との混合を良好
にするノズル条件の設定が必要である。また、耐
火物粉末の吐出条件としては火炎中での充分な滞
留時間を確保し、かつ被補修耐火物表面に衝突す
る際に、充分な運動エネルギーを有するための速
度を確保する必要があり、これを実現する耐火物
粉末の吐出ノズル条件の設定が必要である。 本発明者らはこれらの観点より種々実験を重ね
た結果、液体燃料系溶射器において、液体燃料ノ
ズルは燃料のノズル吐出圧力を1Kg/cm2以上に、
支燃剤の流速を200m/s以上に設定し、粉体吐
出ノズルの条件として、粉体搬送気体の吐出速度
を10m/s以上90m/s以下に設定することが耐
火性に優れた補修施工体を得るために必要である
ことを知見した。 以下、上記各条件の効果について説明する。 まず、液体燃料のノズルは、ノズルの口径、流
量、形状によつて、霧化状況が決定されるが、そ
れらの関係は一般に次式によつて示される。 Q=k.c.d2.√ ここで、Qは流量(m3/min)、kは係数
(−)、cは流量係数(−)、dはノズル口径
(mm)、pはノズル前配管内圧力(Kg/cm2)であ
る。 液体の霧化に用いられるノズルは圧力式噴霧ノ
ズルが用いられ、霧化粒子径を小さくするため
に、ノズル内において流体を旋回する構造のもの
が一般的であるが、ノズルの霧化特性はノズル内
圧力が支配的である。即ち、溶射器においてその
必要な特性である高火炎温を形成するには、ノズ
ル内圧力をある程度以上に高くすることが必要で
ある。 第2図はノズル内圧力と火炎の中心温度および
粉体の供給量に対する付着割合(以下、付着率と
記す)の関係を実験結果により示したものであ
る。 なお、この実験における他の条件は本発明によ
る。図にみられる如く火炎温度は液体のノズル内
圧力が上昇するにつれて高くなり、付着率はノズ
ル内圧力が1Kg/cm2以上の点で耐火物の付着を示
している。 〓〓〓〓
つぎに、支燃剤の効果を第3図に示す。第3図
における支燃剤には酸素を使用し、他の条件は本
発明に従つた。この実験において支燃剤の条件と
して200m/s以上の吐出速度が高温炎の形成と
耐火物の付着に対する効果を示している。 また、粉体搬送ガスの速度は10m/s未満では
被補修面に衝突する際の充分な運動量が得られな
いため、良好な付着状態が得られず、50m/sを
超える速度では火炎内の充分な滞留時間が確保で
きないため、未溶融の状態で被補修面に衝突する
ため、被補修面から粉体が反発する。 また、本発明実施例では、第1図の構造につい
て説明したが本発明はノズル数や配置方法、溶射
器の構造について言及するものではない。 次に実施例により本発明と従来法の補修部の実
積を比較して示す。これより、従来法に比べ特に
気孔率が低く、スラグ耐蝕性に優れた補修部を形
成することが分る。 実施例 表−1に示すMgO主成分の耐火物粉末を酸素
によつて搬送し、搬送用O2の吐出流速を30m/s
とし、噴霧圧1.5Kg/cm2にて灯油をノズルより噴
霧し、ノズルより吐出した流速250m/sの支燃
用酸素により燃焼させ、耐火物粉末を溶融し、耐
火物築造物に付着させた。このときの灯油の使用
量は1400/H、総酸素量は2800Nm3/Hであつ
た。このうち粉末搬送用酸素は400Nm3/H、耐
火物粉末は4T/Hであつた。 因みに補修層厚は20〜40mmであり、これは耐火
物内張の築造に用いたドロマイト煉瓦とほぼ同じ
耐食性を示した。この補修層のサンプルの物性
値、耐食性データを表−2に示す。これより、本
発明による補修部は従来法に比べ、耐食性、強度
において優れた値を示している。
The present invention relates to a method of repairing a refractory-lined structure. Refractory lined structures used in high-temperature furnaces deteriorate, become brittle, and wear out due to thermal or chemical atmospheres during use. For this reason, refractory-lined structures are generally subjected to localized intermediate repairs in order to extend their service life. Normally, intermediate repairs of these refractory-lined structures are carried out by pouring and molding a monolithic refractory made by mixing powdered refractories with water, or by spraying it onto the surface to be repaired. In order to carry out the work, thermal spalling of the refractories due to the temperature drop and rise of the high-temperature building is unavoidable, and the strength of the repaired part is weak. Also, if you try to do this hot, you will have to apply it to the surface to be repaired in the high temperature area.
Poor adhesion, high porosity due to water evaporation,
Fire resistance is poor. In addition, in recent years, as a new method of repairing refractories,
Thermal spray repair methods using refractory powder are being adopted for some refractory structures, but up to now powder spraying methods have mainly been carried out using gaseous fuels and solid fuels. Ta. In powder spraying methods that use gaseous fuel, low molecular weight hydrocarbon compounds such as LNG, LPG, and acetylene are used as fuel, so the flame temperature is generally low and MgO
Because it cannot melt high-melting-point refractories such as
The range of application was limited due to the relatively small capacity of about 500 kg/H. Additionally, there is a danger associated with abnormal combustion of the gaseous fuel and the combustion-supporting mixture such as oxygen. On the other hand, in thermal spraying methods that use solid fuels such as coal and coke powder, the reaction time required for the combustion reaction is long, resulting in the formation of a long flame at a low temperature, making it impossible to melt high melting point materials such as MgO. In addition, ash (SiO 2 ,
(Fe 2 O 3 , Al 2 O 3, etc.), i.e. refractoriness〓〓〓〓
It had the disadvantage of a decrease in As mentioned above, conventional methods for repairing refractory-lined structures are inherently low in fire resistance when wet repairing monolithic refractories, and conventional thermal spray repair methods cannot melt high-melting point materials. For,
It is not possible to form a construction body with low porosity, high density, high melting point, and high fire resistance, and although it is superior to the wet method in terms of corrosion resistance, it still has drawbacks such as frequent repairs and a small range of application. The present invention relates to a method for repairing a refractory lined structure that improves the drawbacks of the conventional thermal spraying method as described above and forms a refractory repair surface having low porosity, high density, high melting point, and high fire resistance. . The present invention provides for the repair of refractory-lined structures,
Liquid fuel is sprayed from a nozzle at a spray pressure of 1 Kg/cm 2 -G (hereinafter simply referred to as 1 Kg/cm 2 ) or more in the pipe, and oxygen is added as a combustion agent for the sprayed liquid fuel at a flow rate of 200 m/s or more. Use a powder sprayer with a three-fluid nozzle hole that supplies refractory powder carried by oxygen into the flame discharged from the nozzle and burned at a carrier gas velocity of 10 m/s or more and 90 m/s or less. By repairing the refractory material, a refractory repair surface having low porosity, high density, high melting point, and high fire resistance is formed. Hereinafter, one embodiment of the present invention will be described with reference to the drawings. FIG. 1 shows a powder spraying apparatus according to an embodiment of the present invention. In the figure, 1 is a nozzle for a combustion supporting agent such as oxygen, and 2 is a powder injection nozzle that discharges refractory powder conveyed by oxygen or air. 3 is a liquid fuel injection nozzle, and in order to reduce the diameter of the atomized droplets, the powder is distributed to each nozzle by the distributor 5. A nozzle with a swirler at the tip and a constricted tip is used. It will be done. 4
is a cooling cylinder, which includes a flow path for cooling water. In order to melt the refractory powder in a flame in a powder sprayer and adhere it to the refractory lining, it is necessary to raise the flame temperature above the melting point of the refractory powder. Incidentally, the combustion condition of liquid fuel, that is, the properties of the flame, are determined by the condition of the atomized fuel droplets and the mixing condition of the droplets and the combustion support agent.In order to increase the flame temperature, the diameter of the fuel droplets must be adjusted. It is necessary to make the area of contact with the combustion support agent small by increasing the contact area with the combustion support agent, and to improve the mixing of the fuel and the combustion support agent. Therefore, in order to spray high melting point refractory powder,
In a liquid fuel type thermal sprayer, it is necessary to set nozzle conditions that reduce the diameter of atomized liquid fuel droplets and improve the mixing of the fuel and combustion agent. In addition, the discharge conditions for the refractory powder include ensuring sufficient residence time in the flame, and ensuring a velocity that provides sufficient kinetic energy when colliding with the surface of the refractory to be repaired. It is necessary to set the refractory powder discharge nozzle conditions to achieve this. As a result of various experiments carried out by the present inventors from these points of view, in a liquid fuel type thermal sprayer, the liquid fuel nozzle has a fuel nozzle discharge pressure of 1 kg/cm 2 or more,
A repair work with excellent fire resistance can be achieved by setting the flow velocity of the combustion support agent to 200 m/s or more, and setting the discharge velocity of the powder carrier gas to 10 m/s or more and 90 m/s or less as a condition for the powder discharge nozzle. We found that it is necessary to obtain The effects of each of the above conditions will be explained below. First, the atomization state of a liquid fuel nozzle is determined by the aperture, flow rate, and shape of the nozzle, and the relationship therebetween is generally expressed by the following equation. Q=kcd 2 .√ Here, Q is the flow rate (m 3 /min), k is the coefficient (-), c is the flow coefficient (-), d is the nozzle diameter (mm), and p is the pressure in the pipe in front of the nozzle ( kg/cm 2 ). The nozzle used to atomize liquid is a pressure-type atomizing nozzle, which generally has a structure in which the fluid is swirled within the nozzle in order to reduce the atomized particle size, but the atomization characteristics of the nozzle are The pressure inside the nozzle is dominant. That is, in order to form a high flame temperature, which is a necessary characteristic in a thermal sprayer, it is necessary to increase the pressure inside the nozzle to a certain level or higher. FIG. 2 shows the relationship between the nozzle internal pressure, the center temperature of the flame, and the adhesion rate (hereinafter referred to as the adhesion rate) with respect to the amount of powder supplied, based on experimental results. Note that other conditions in this experiment were according to the present invention. As seen in the figure, the flame temperature increases as the nozzle internal pressure of the liquid increases, and the adhesion rate indicates that refractory material adheres at a point where the nozzle internal pressure is 1 Kg/cm 2 or more. 〓〓〓〓
Next, the effect of the combustion stabilizer is shown in Fig. 3. Oxygen was used as the combustion agent in FIG. 3, and other conditions were in accordance with the present invention. In this experiment, a discharge speed of 200 m/s or more was effective for the formation of high-temperature flames and the adhesion of refractories. In addition, if the velocity of the powder carrier gas is less than 10 m/s, sufficient momentum will not be obtained when it collides with the surface to be repaired, so a good adhesion state will not be obtained, and if the velocity exceeds 50 m/s, the Since sufficient residence time cannot be secured, the powder collides with the surface to be repaired in an unmelted state, and the powder is repelled from the surface to be repaired. Further, in the embodiments of the present invention, the structure shown in FIG. 1 has been described, but the present invention does not refer to the number of nozzles, the arrangement method, or the structure of the thermal sprayer. Next, an example will be shown to compare the actual amount of repaired parts of the present invention and the conventional method. It can be seen from this that a repaired part with particularly low porosity and excellent slag corrosion resistance can be formed compared to the conventional method. Example: The refractory powder mainly composed of MgO shown in Table 1 was transported by oxygen, and the delivery flow rate of O 2 for transport was 30 m/s.
Then, kerosene was sprayed from a nozzle at a spray pressure of 1.5 kg/ cm2 , and combustion was caused by combustion-supporting oxygen discharged from the nozzle at a flow rate of 250 m/s to melt the refractory powder and adhere it to the refractory structure. . The amount of kerosene used at this time was 1400/H, and the total amount of oxygen was 2800 Nm 3 /H. Of these, the oxygen for powder transportation was 400Nm 3 /H, and the amount of refractory powder was 4T/H. Incidentally, the thickness of the repair layer was 20 to 40 mm, which showed almost the same corrosion resistance as the dolomite bricks used to construct the refractory lining. Table 2 shows the physical properties and corrosion resistance data of this repair layer sample. This shows that the repaired area according to the present invention has superior corrosion resistance and strength compared to the conventional method.

【表】【table】

【表】【table】 【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例による溶射装置を示
したもので、aは軸方向断面図、bは軸方向と直
交断面図、第2図はノズル内圧力と火炎の中心温
度および粉体の供給量に対する付着率の関係線
図、第3図は支燃剤の効果を示す関係線図であ
る。 1……支燃剤吐出ノズル、2……粉体吐出ノズ
ル、3……液体燃料ノズル、4……冷却剤流通
路、5……粉体入口、6……液体燃料入口、7…
…支燃剤入口、8……冷却剤入口、9……冷却剤
出口。 〓〓〓〓
Fig. 1 shows a thermal spraying apparatus according to an embodiment of the present invention, in which a is an axial sectional view, b is a sectional view orthogonal to the axial direction, and Fig. 2 shows nozzle internal pressure, flame center temperature, and powder. FIG. 3 is a relationship diagram showing the effect of the combustion-supporting agent. DESCRIPTION OF SYMBOLS 1... Combustion support agent discharge nozzle, 2... Powder discharge nozzle, 3... Liquid fuel nozzle, 4... Coolant flow path, 5... Powder inlet, 6... Liquid fuel inlet, 7...
... Combustion agent inlet, 8... Coolant inlet, 9... Coolant outlet. 〓〓〓〓

Claims (1)

【特許請求の範囲】[Claims] 1 耐火物内張築造物の築造において、液体燃料
をノズルから1Kg/cm2以上の噴霧圧により噴霧さ
れた液体燃料の支燃剤として酸素を200m/s以
上の流速でノズルより吐出させて燃焼させた火炎
中に、気体により搬送された耐火物粉末を10m/
s以上90m/s以下の速度でノズルにより供給す
る三種流体のノズルの吐出孔を有する粉末溶射器
により補修することを特徴とする耐火物内張築造
物の補修方法。
1. In the construction of refractory-lined structures, liquid fuel is sprayed from a nozzle at a spray pressure of 1 kg/cm 2 or more, and oxygen is discharged from the nozzle at a flow rate of 200 m/s or more as a combustion support agent for combustion. The refractory powder transported by gas was
1. A method for repairing a refractory-lined structure, characterized in that the repair is carried out using a powder sprayer having a nozzle discharge hole for supplying three types of fluids through a nozzle at a speed of not less than 100 m/s and not more than 90 m/s.
JP14334282A 1982-08-20 1982-08-20 Method of repairing refractory lining building Granted JPS5935775A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14334282A JPS5935775A (en) 1982-08-20 1982-08-20 Method of repairing refractory lining building

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14334282A JPS5935775A (en) 1982-08-20 1982-08-20 Method of repairing refractory lining building

Publications (2)

Publication Number Publication Date
JPS5935775A JPS5935775A (en) 1984-02-27
JPS6135466B2 true JPS6135466B2 (en) 1986-08-13

Family

ID=15336553

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14334282A Granted JPS5935775A (en) 1982-08-20 1982-08-20 Method of repairing refractory lining building

Country Status (1)

Country Link
JP (1) JPS5935775A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2170122B (en) * 1985-01-26 1988-11-30 Glaverbel Process of forming a refractory mass and lance for spraying particulate exothermically oxidisable material
JP6422101B2 (en) * 2013-12-25 2018-11-14 Jfeスチール株式会社 Thermal spray repair method for furnace wall

Also Published As

Publication number Publication date
JPS5935775A (en) 1984-02-27

Similar Documents

Publication Publication Date Title
US4192460A (en) Refractory powder flame projecting apparatus
CN1122780C (en) Granule jetting burner
JP2010261714A (en) Liquid fuel type hvof thermal spray gun and burner design
CN107904541A (en) A kind of supersonic flame spraying method and spray equipment
JP3189729B2 (en) Thermal spray equipment for refractory repair and repair method by thermal spraying of refractory
CN101375100A (en) Flat-flame furnace top burner with low pollutant discharge
JPS6135466B2 (en)
EP0745428B1 (en) Flame spraying burner
CN1252018A (en) Lance for heating or ceramic welding
US20100215864A1 (en) Method of high intensity cooling of permeable burner block of a flame spray apparatus
JPH11237007A (en) Combustion furnace and combustion method for combustion or flame hydrolysis
JPH09248497A (en) Refractory thermal spraying method and apparatus
JPS5951857B2 (en) Powder refractory spraying method
JP7056927B2 (en) Combustion mechanism that enables ignition and stable flame in HVAF thermal spraying equipment
KR200243640Y1 (en) flame melting injection oxygen bunner of cooling type
CN207596939U (en) A kind of supersonic flame sprayer
JP3035564B2 (en) Oxygen-enriched oil combustion method
JPH059513A (en) Method for preventing clogging of molten metal on fluid jet nozzle and its protection guide
JPS627412Y2 (en)
JP2886070B2 (en) Hot spray repair nozzle
JP2001214252A (en) High-speed thermal spray apparatus for forming a substance and a method for forming a coating or a bulk substance by the spray apparatus
JPS646930Y2 (en)
JP3513963B2 (en) Flame spray repair material
JPS6046062B2 (en) Refractory materials for thermal spraying
JPS6248156B2 (en)