METHOD AND APPARATUS FOR SPRAY COATING OF REFRACTORY MATERIAL TO REFRACTORY CONSTRUCTION

Abstract: Device with a lance (10) having two nozzles (12, 14) for the use in spray coating of refractory constructions. The spray coating is performed utilizing a mixture of refractory material and a combustionable metal powder. The size of the particle of the metal in the mixture is selected so that the particle size is large enough to be treated safely and is small enough to be transported by means of a gas flow. As a carrier gas for carrying the mixture, a non-combustionable gas or fuel gas is used. A fuel gas and a combustion-assisting gas are discharged toward the section to be treated on the surface for directing a combustioning frame. The refractor material with the carrier gas is discharged into the frame established by the fuel gas and the combustion-assisting gas. This compensates combustion efficiency to be dropped by utilizing the larger particle size metal.

Description: BACKGROUND OF THE INVENTION Field of the Invention The present invention relates generally to a method and device for safely performing spray coating of a refractory material onto a refractory construction. More specifically, the invention relates to performing a safe and effective repair of refractory constructions, such as coke ovens, kilns furnaces and so forth. Further particularly, the invention relates to a spray coating technic avoiding danger in spray coating of the refractory material containing fine particles of powder state combustible metal. Description of the Background Art Coke ovens, kilns, furnaces employ refractory linings for constituting refractory constructions so as to allow substantially high temperature operations. Such refractory linings are subjected to substantially high temperature for a long period of time thus causing hot tear, spalling, formation of defects, cracks and so forth. As it is well known, the coke oven and some kind of furnaces, such as brust furnace, have to be in operation continuously throughout their lives. Accordingly, repair of such hot tears, spalling, defects, cracks and so forth is to be preformed without stopping the operation. Conventionally repairing operations for the refractory linings have been taken place by way of spray coating. Such spray coating process has been disclosed in the Japanese Patent Second (examined) Publication (Tokko) Showa 49-46364. In the disclosed process, a refractory material is selected to have same composition to that of the refractory lining to be repaired. The refractory material is mixed with a certain amount of fine particle of powder state combustible metal. In the spray coating operation, heat generated by combustion of the metal powder is utilized for melting or half-melting the refractory material and for adhering the refractory material onto the refractory lining. At the same time, the metal oxide formed as a resultant of combustion also serves as refractory material. In such a conventional spray coating process, it is considered that a caloric value required for performing spray coating of refractory material for repairing refractory linings is in a range of 5000 kcal/kg to 8000 kcal/kg, as recited in ''Spray Coating Repair of Coke Oven'' (Seitetsu Kenkyu Vol. No. 305), published on 1981, and ''Development of Spray Coating Apparatus and Study of Spray Coating Condition'' (''Iron and Steel'' No. 4, Vol. No. 169), 1983. The caloric value which may be generated according to the process recited in the afore-mentioned publications is only in a range of 2000 kcal/kg to 3000 kcal/kg. The proposed process thus includes inclusion of 20 Wt% to 30 Wt% of metal particles in the refractory material to form a mixture, which metal particles will serve as combustion medium. However, the caloric value to be generated by the proposed process is too small to melt or half-melt the refractory materials to be injected onto the surface of the refractory lining. This degrades adherence ability of the refractory material onto the reflactory lining. Furthermore, due to lack of caloric value, formation of satisfactorily high density refractory layer and firm adherence of the formed refractory layer on the refractory lining have been difficult. It would be possible to increase caloric value of the heat to be generated during combustion by increasing the concentration of the metal powder. However, increasing the amount of the metal powder concentration apparently causes increasing of the cost required for repairing. In addition, in the prior proposed process, the particle size of the metal powder is limited in diameter to be smaller than 50 µm. The metal powder having the aforementioned limited particle size is carried by oxygen flow. This makes difficult the practical process due to high combusibility of such fine particles of metal, which causes danger in carrying and back-fire in spray coating process. Furthermore, since the calories for spray coating are generated only by combustion of the metal particles in the aforementioned prior art, the refractory lining to be repaired cannot be heated in advance of starting spray coating. As a result, the refractory lining to be treated is rapidly heated at a spot. The heating spot of the refractory lining is rapidly cooled when the spray coating operation is terminated. This tends to cause spalling in the refractory construction to be repaired. SUMMARY OF THE INVENTION Therefore, it is an object of the present invention to provide a method and a device for spray coating of refractory material, which can perform operation safely and effectively. Another object of the invention is to provide a method and a device for spray coating of refractory material onto a surface of a refractory construction, which allows relatively great particle size metal to be used. A further object of the invention is to provide a method and a device for spray coating, which can form a flame directed toward the surface to be treated, independently of the spray coating operation for allowing moderate warming-up and cooling-off of the surface of the refractory construction in order to prevent the portion to be treated from causing spalling. In order to accomplish the aforementioned and other objects, a method of spray coating, according to the present invention, is performed utilizing a mixture of refractory material and a relatively large average particle size of powder state combusible metal. This method is disclosed in claim 1. Additional features are disclosed in subclaims 2 to 20. The features of the device for carrying out the method according to the invention are disclosed in claims 21 to 29 The size of the particle of the metal in the mixture is selected so that the particle size is large enough to be treated safely and is small enough to be transported by means of a gas flow and to be effectively combusted without requiring substantial increase of the cost. As a carrier gas for carrying the mixture, a non-combustible gas or fuel gas and other non-oxidizing gas can be used. A fuel gas and an oxygen containing combustion-assisting gas, such as oxygen gas, air and so forth, are discharged toward the section to be treated on the surface for directing a combustion flame. The refractory material with the carrier gas is discharged into the flame established by the fuel gas and the combustion-assisting gas. In view of the safety in operation, the size of the metal powder to be used in the spray coating according to the invention, is limited to be greater than 50 µm in diameter. By enlarging the particle size of the metal, combustibility of the metal powder is lowered. Combustion of such large particle size metal can be assisted by discharging the combustion-assisting gas together with the fuel gas. This compensates combustion efficiency to be dropped by utilizing the larger particle size metal. Furthermore, according to the present invention, caloric value to be generated by combustion of the metal within the flame established by the combustion gas and the combustion-assisting gas, becomes sufficient for melting or half-melting the refractory material on the surface of the refractory construction to be treated. The metal oxide formed during combustion in the flame will form a mixture with the refractory material, as an additional refractory material. Therefore, it enables to form satisfactorily high density of refractory layer on the section to be treated. BRIEF DESCRIPTION OF THE DRAWINGS The present invention will be understood more fully from the detailed description given herebelow and from the accompanying drawings of the preferred embodiment of the invention, which, however, should not be taken to limit the invention to the specific embodiment but are for explanation and understanding only. In the drawings: Fig. 1 is a schematic diagramatic illustration showing the preferred embodiment of a spray coating device according to the invention; Fig. 2 is a graph showing relationship between a refractory layer adhering efficiency and average particle size of a metal particle to be mixed with a refractory material; Fig. 3 is a graph showing relationship between porosity in the refractory layer established and the average particle size of the metal particle contained in the mixture; Fig. 4 is a graph showing relationship between a refractory layer adhering efficiency and a concentration of the metal particle in a mixture of the refractory material and the particle metal; Fig. 5 is a graph showing relationship between porosity and amount of the metal particle in the refractory material mixture; Fig. 6 is a graph showing relationship between porosity in the established refractory layer and oxygen supply rate; Fig. 7 is a graph showing relationship betweeen porosity and average particle size of the metal particle when combustion gas is not supplied; Fig. 8 is graph showing relationship between porosity and average particle size of the refractory article to be utilized in the preferred embodimenr of Fig. 1; Fig. 9 is a schematic and diagramatic illustration showing a modification of the preferred embodiment of the spray coating device of Fig. 1; and Fig. 10 is a schematic and diagramatix illustration showing another modification of the preferred embodiment of the spray coating device of Fig. 1. DESCRIPTION OF THE PREFERRED EMBODIMENT Referring now to the drawings, particularly to Fig. 1, the preferred embodiment of a spray coating apparatus, according to the present invention, has a lance 10. The lance 10 has an inner injection nozzle 12 and an outer injection nozzle 14. The inner injection nozzle 12 extends axially along tee center axis of the lance 10. On the other hand, the outer injection nozzle 14 is in an annular form and arranged coaxially with the inner injection nozzle 12. The inner and outer injection nozzles 12 and 14 are directed toward the surface of a refractory wall or refractory lining 11. In Fig. 1, the refractory wall 11 has a defect 13 on the surface. In order to perform repairing for filling the defect with the refractory material, the inner and outer injection nozzles 12 and 14 of the lance 10 are specifically directed to the defect 13 in order to perform spray coating for filling the defect with the refractory material. The inner injection nozzle 12 is connected to a refractory material supply line 16, which is connected to an ejector feeder assembly 18 at the end remote from the lance 10. To the ejector feeder assembly, a carrier gas source 20 is connected via a non-combustible gas supply line 22 and a carrier gas flow control valve 24. According to the preferred embodiment of the spray coating device, the carrier gas source 20 is designed to supply a pressurized inert gas or non-combustible gas through the carrier gas supply line 22. On the other hand, the ejector feeder assembly 18 has a suction pipe 26 inserted into a hopper 28 filled with a mixture of a refractory material and fine particles of powder state combustible metal. A refractory material flow control valve 30 is disposed within the refractory material supply line 16 for establishing and blocking communication between the lance 10 and the ejector feeder assembly 18 so as to control supply of refractory material to the inner injection nozzle 12 of the lance 10. A branch line 32 of the carrier gas supply line 22 is connected to the hopper 28 to introduce therein the inert or non-combustible gas. Also, a fuel gas supply line 34 for supplying a non-oxidizing fuel gas, such as propane and the like, connects the refractory material supply line 16 upstream of the lance 10 to a fuel gas source 36. A fuel gas flow control valve 38 is disposed in the fuel gas supply line 34 for establishing and blocking communication between the refractory material supply line 16 and the fuel gas source 36. The outer injection nozzle 14 is connected to a combustion-assisting gas source 40 via a assisting gas supply line 42 and a assisting gas flow control valve 44 for discharging a oxygen containing combustion-assisting gas, such as oxygen gas, air and the like. The assisting gas flow control valve 44 establishes and blocks communication between the combustion- assisting gas source 40 and the outer injection nozzle 14 of the lance 10. A cooling water passage 46 is defined within the peripheral wall of the lance 10 or surrounding the outer injection nozzle 14. The cooling water passage 46 is connected to a cooling water source 48 via cooling water supply line 50 and a cooling water supply control valve 52. A drain line 54 with a drain control valve 56 is also disposed between the cooling water passage 46 and the cooling water source 48. Therefore, the cooling water supplied from the cooling water source 48 is circulated through the cooling water passage 46 for cooling the lance 10. The carrier gas flow control valve 24, the refractory material flow control valve 30, the fuel gas flow control valve, the assisting gas flow control valve. the cooling water supply control valve 52 and the drain control valve 56 are respectively associated with electrically operable actuators 58, 60, 62, 64, 66 and 68. Respective actuators 58, 60, 62, 64, 66 and 68 are controlled by control signals produced by a control unit 70. In the shown embodiment, the N₂ gas is used as the non-combustible carrier gas. As a fuel gas, propane gas, acetylene gas and so forth can be used. On the other hand, as the combustion-assisting gas, oxygen or atmospheric air as oxygen containing gas is used. The refractory material is selected among silica, alumina, mullite, chamotte, zircon, zirconia, magnesia, magnesite-chrome and so forth, or the combination thereof. The refractory material is selected from the above, according to the composition of the refractory wall 11 to be treated. The metal to be mixed with the refractory material set forth above is selected among, aluminium, metallic silicon and the combination thereof. Also, Mg, Mn, FeMn, SiMn, CaSi, FeSi, FeCr, CaC₂ and the combinations thereof can be used as metal. As set forth, when the metal powder in the average particle size less than 50 µm in diameter, the combustibility of the metal powder is substantially high to be easily combusted. This requires substantially careful attention in transportation and in spray coating operation so as to avoid danger in accidental combustion or back-firing. Even when a substantially high attention is paid, the operator may still be in danger. In view of safety in handling and operation, the average particle size of the metal powder has to be greater than 50 µm. On the other hand, in the shown device, the metal powder is carried with the refractory material by means of the non-combusible gas flow. Therefore, the maximum size of the metal particle is limited in view of the flow velocity and pressure of the non-combustible gas as the carrier gas. Furthermore, as is well known, a larger particle size metal powder has lower combustibility. Therefore, if the average particle size of the metal powder becomes excessively large, it will cause difficulty in generating satisfactory combustion during spray coating operation. This, in turn, means that the adherence ability of the refractory layer to be formed by the spray coating will be differentiated depending upon the average particle size of the metal powder. Fig. 2 shows variation of the adhering ability with respect to various average particle sizes of the metal powder. It should be noted that Fig. 2 shows a result of experimentation take place utilizing powder state aluminium as the material of combusible metal. In the experimentation, propane gas is utilized for supplying various caloric values by combustion thereof. Namely, amount of the propane gas is adjusted to provide caloric values 0 kcal, 2000 kcal, 3000 kcal and 4000 for 1 kg of the mixture of the refractory material and the metal particles. In the mixture, 15% by weight of the metal powder, i.e. aluminium powder, is contained. In Fig. 2, line A shows the variation of the adherence ability (Wt%) of the refractory layer established when the amount of propane is adjusted to provide 0 kcal of caloric value. Likewise, lines B, C and D respectively show adherence ability at 2000 kcal, 3000 kcal and 4000 supplied by combustion of the propane gas. As observed from Fig. 2, when 3000 kcal of caloric value is supplied, relatively high adherence ability was obtained when the average particle size of the aluminium powder is less than or equal to 160 µm. Namely, the adherence ability at the average particle size 160 µm of the aluminium particles with providing the 3000 kcal of calory corresponds to that of the particle size 20 µm of the aluminium powder providing no calory. Therefore, in view of the result of experimentation set forth above, the maximum average size of the metal powder is preferred at the average size less than or equal to 160 µm. Fig. 3 shows porosity in the refractory layer formed in the experimentation set forth above. In Fig. 3, the lines A, B, C and D respectively show porosity of the refractory layer formed by spray coating operations with providing calory of 0 kcal, 2000 kcal, 3000 kcal and 4000 kcal by combustion of the propane gas. As observed from Fig. 3, while the average particle size in diameter of the aluminium powder is held smaller than or equal to 160 µm, the porosity is maintained less than or equal to 20%. In view of this, the particle size of the metal powder is also preferred at the average size less than or equal to 160 µm. In further observation in Fig. 3, it would be appreciated that it would be more preferable to limit the range of average particle size of the metal powder in diameter less than or equal to 140 µm. Therefore, in view of the preferred porosity, it would be appreciated that it is more preferabe to limit the range of the average metal particle size to 70 µm to 140 µm. Fig. 4 shows variation of adherence ability of the refractory layer formed by spray coating in relation to the content of the metal powder. In order to find an optimum content of the metal powder in the mixure of the refractory material and the metal powder, an experimentation was performed. For this experimentation, the average particle size 80 µm in diameter of the aluminium powder is utilized to be mixed with the refractory material. For experimental spray coating operation, supply calory was adjusted at 1000 kcal. As seen from Fig. 4, the adherence ability is icnreased at substantially high rate according of increasing of the content of the aluminium powder upto 10 Wt%. After reaching 10 Wt% increasing rate of the adherence ability is substantially lowered. In view of the result of experimentation as shown in Fig. 4, it will be appreciated that satisfactory adherence can be obtained when the content of the metal powder is greater than or equal to 10 Wt%. On the other hand, as will be naturally understood, increasing of the amount of the metal powder increases the cost of spray coating. Therefore, in view of the cost-vs- performance. the preferred range of metal powder content is in a range of 10 Wt% to 30 Wt%. Fig. 5 shows variation of porosity in the refractory layer formed by spray coating with various content of the metal powder. As seen from the graph of Fig. 5, the porosity is held lower than or equal to 20% when the content of the metal powder in the refractory material mixture is in a range of 10% to 30 % by weight. This may confirm that the content of the metal particle in the range of 10 Wt% to 30 Wt% is preferred. In the further obsevation, it is appreciated that when the content of the metal powder in the mixture of the refractory material and the metal powder is higher than about 15 Wt%, the porosity becomes less than or equal to 10%. In additionally considering the cost-vs-performance, the further preferred range of the content of the metal powder is in a range of 13 WT% to 20 WT%. As will be appreciated, it is preferable to completely combust the metal powder to generate caloric value sufficient for melting or half-melting the refractory material and to convert the combustible metal into refractory metal oxide. The particles of metal oxide in a melt or half-melt state coat the outer periphery of the refractory material which is also in melt or half-melt state. In order to obtain complete combustion of the combustible metal particle, sufficient amount of combustion-assisting gas, such as oxygen, air and so forth, is required. In order to determine the supply ratio of the combustion-assisting gas, an experimentation is performed. In the experimentation, alumina refractory which has a composition of 85 Wt% of Al₂O₃, 10 Wt% of SiO₂ and remainders of Fe₂O₃, CaO. The alumina refractory is mixed with aluminium particles having an average particle size of 100 µm. The aluminium particles are contained in the refractory material mixture in a rate of 10% by weight. As the combustion-assisting gas, oxygen was used and as the fuel gas, propane was used. Amount of propane was adjusted to generate 3500 kcal of caloric value in total including caloric value generated by combustion of the aluminium powder. The graph in Fig. 6 shows variation of the porosity in the refractory layer formed in the experimentation in relation to the oxygen supply ratio relative to the theoritical equivalent amount of oxygen for oxidation of the aluminium powder. It should be noted that equivalent amount of oxygen for combustion of propane gas was neglected from the value in the graph. As observed from Fig. 6, porosity of the refractory layer formed in the aforementioned experimentation is held less than or equal to 20% when the supply rate of the oxygen is three-times or more of the theoritical equivalent amount. The porosity of the refractory layer can be held lower than or equal to 20% as increasing the oxygen supply rate upto fifteen-times of the theoritical equivalent. When the oxygen supply rate exceeds fifteen-times of the theoritical equivalent, the porosity again increases. As will be appreciated herefrom, the oxygen supply rate is preferably in a range of three-times to fifteen times of the equivalent amount relative to the amount of the aluminium powder in the refractory material mixture. As will be further seen from Fig. 6, the further preferable oxygen supply rate is four-times to fifteen times of the theoretical equivalent. On the other hand, as will be easily appreciated, the adherence ability of the refractory layer to be formed is variable depending upon the magnitude of melting of the refractory material. The melting magnitude of the refractory material will be increased by increasing the caloric value to be provided thereto. Therefore, in order to satisfactorily melt the refractory material, sufficient amount of fuel gas to generate sufficient caloric value, has to be supplied. As set forth, in order to obtain satisfactory melting magnitude, 5000 kcal to 8000 kcal of caloric value is required in the prior art as set forth above. This requires large amount of fuel gas to make the spray coating expensive. According to the present invention, since the additional caloric value is provided by combustion of the metal powder, required fuel amount can be reduced. In the present invention, the fuel gas amount to be supplied in the spray coating operation is set for providing less than or equal to 5000 kcal of caloric value during combustion for 1 kg of refractory material. More preferable range of caloric value to be generated by combustion of the fuel gas is 2000 kcal to 4000 kcal per 1 kg of refractory material. By providing such reduced amount of fuel gas, the caloric value to be generated in combustion of the fuel gas in the frame become insufficient to cause melting of the refractory material. Therefore, the refractory material discharged through the lance 10 will be merely heated to be easily melted by providing additional calory. In observation of the process of formation of the refractory layer according to the invention, it was found that the not molten particles of refractory material contact onto the surface of the refractory construction to be treated, with the combusting particles of metal powder. On the surface of the refractory construction, the metal powder particles continue combustion to directly transmit the combustion calory to the refractory material. Calory transmission efficiency from the combustion metal to the refractory material is much higher than that transmitted from the combustion gas to the refractory maetrial. As a result, the retractory material on the surface of the refractory construction melts and/or half-melts to successfully adhere on the associated surface of the refractory construction. If the caloric value sufficient for melting and/or half-melting the refractory material in the combustion flame is provided, part of the molten refractory material adheres onto the internal periphery of the inner nozzle of the lance to cause variation of the path area of the nozzle. This causes fluctuation of the injection rate of the refractory material, the metal powder and the fuel gas to vary performance of the spray coating. This will be seen from lines G and H in Fig. 8. The lines G and H are obtained from the experimentation set forth above by providing 5000 kcal and 6000 kcal of caloric value. As will be clear herefrom, the preferred range of the fuel gas supply amount in the present invention is to generate less than or equal to 5000 kcal, and more preferably 2000 kcal to 4000 kcal. Returning to Fig. 1, the practical spray coating operation to be taken place by the preferred embodiment of the spay coating apparatus according to the invention will be disclosed herebelow. In order to prevent the refractory wall from causing spalling, it would be preferable to gradually and moderately heat the refractory wall in advance of performing spray coating. Therefore, control unit 70 feeds the control signals to the actuators 62 and 64. As a result, the actuators 62 and 64 become active to open the aasociated fuel gas supply control valve 38 and the assisting gas supply control valve 44. Therefore, the fuel gas source 36 and the combustion-assisting gas source 40 are connected to the inner and outer injection nozzles 12 and 14 of the lance 10. Since the lance 10 is inserted into the substantially high temperature atmospher in the coke oven, kiln, furnace or so forth, the fuel gas is burnt or combustioned to establish a frame directed toward the defect 13 on the refractory wall 11. By the flame established as set forth above, the portion of the refractory wall 11 to be treated is heated beforehand of starting spray coating. Subsequently, the control signal is transmitted to the actuator 58 to open the carrier gas flow control valve 24 to establish communication between the carrier gas source 20 and the ejector feeder assembly 18. By opening of the carrier gas flow control valve 24, the pressurized non-combustible carrier gas is introduced into the hopper 28 to increase the internal pressure of the hopper. After the pressure in the hopper reaches a predetermined value, the control signal is fed to the actuator 60 to open the refractory material flow control valve 30. Therefore, pressurized carrier gas starts to flow through the ejector feeder assembly 18 and the refractory material supply line 16. During passing of the non-combustible carrier gas through the ejector feeder assembly 18, the mixture of the refractory material and the metal powder is drawn into the ejector feeder assembly and transferred through the refractory material supply line 16. Therefore, the refractory material mixture flows through the refractory material supply line. Since the fuel gas is introduced into the refractory material supply line 16 at the position downstream of the refractory material flow control valve 30 and upstream of the inner injection nozzle 12 of the lance, a combustible mixture of the refractory material, the combustible metal powder and the fuel gas is established. The combustible mixutre containing the fuel gas is transferred into the inner injection nozzle. Upon being injected from the end of the inner injection nozzle 12, the refractory material mixture and the fuel gas subject substantially high atmospher to establish combustion. At the same time, the combustion-assisting gas is discharged through the end of the outer injection nozzle 14 around the flame established by combustion of the metal powder in the refractory material mixture and the fuel gas. By the presence of the combustion-assisting gas, combustion flame propagates. The refractory material with combusting metal powder contacts onto the surface of the refractory wall 11, on which the defect 13 is formed. At this time, the metal oxide as a resultant of the combustion may also serve as the refractory material and is mixed with the refractory material. This increases density of the refractory material to increase the density of the refractory layer formed by the spray coating. After completing required spray coating operation, the control signals are transmitted to the actuators 58 and 60 to close the carrier gas flow control valve 24 and the refractory material flow control valve 30. As a result, supply of refractory material is shut. At this time, since the fuel gas flow control valve 38 and the assisting gas flow control valve 44 are kept open, combustion of the fuel gas is maintained to enable to gradually and moderately cool off the refractory wall. This successfully prevents the refractory wall from causing spalling. EXAMPLE I Utilizing the preferred embodiment of the spray coating device of Fig. 1, the repair is performed for fire brick construction around a tuyere of a hot metal ladle having hot metal receiving capacity of 100t. The fire blick was made of high alumina material. Repairing operation is performed by spray coating by injecting mixture of the refractory material and the metal particle in amount of 60 kg/h. The flow of the combustion-assisting gas, i.e. oxygen flow, is established around the mixture injected. Aluminium powder was used as the combusible metal component of the mixture. Maximum particle size of the aluminium powder was 120 µm and the average particle size was 80 µm. This aluminium powder was mixed with a alumina refractories having maximum average particle size of 500 µm. The alumina refractories has a composition of 87 Wt% of Al₂O₃ and remainders is constituted of SiO₂, CaO, Fe₂O₃. The aluminium powder and alumina refractories were mixed at a mixture ratio of 20 : 80 by weight. The wall of the ladle to be repaired was previously heated by a flame established by combustion of propane gas (C₃H₈) as the fuel gas, at a temperature of 1400 °C. After the wall temperature reaches about 1400 °C, the mixture was introduced into the lance for injection with N₂ gas as the non-combisible carrier gas. To the flow of the mixture and N₂ gas, the propane gas is introduced in amont of 6.0 m³/h. The combustion-assisting gas, i.e. oxygen, is also discharged around the mixture injected. The discharge rate of the combustion-assisting gas was set at 37.5 m³/h. Spray coating operation was continued for about 10 minutes. As a result, satisfactory refractory layer could be formed on the fire brick. Spalling was not observed in the fire brick. Furthermore, as observed the established refractory layer, the layer was firmly adhered on the fire brick. After completing the aforementioned repairing operation, the hot metal ladle thus repaired was used to receive 100t of hot metal at the temperature of 1650 °C. The received hot metal was transported to a station where continuous casting is performed and poured into a continuous caster from the ladle. The repaired ladle could be used for 6 heats of the foregoing operations. EXAMPLE II In order to compare the efficiency and performance of the spray coating according to the invention, comparative experimentation was performed. The comparative experimentation has been performed without supplying the combustion-assisting gas, such as oxygen or air, according to the process set out in the Japanese Patent Second Pulication 49-46364. Fig. 7 shows variation of porosity of the refractory layer formed during the comparative experimentation. Content of aluminium powder was varied in various samples to the rates of 10 Wt%, 15 Wt% and 20 Wt%. As will be seen from Fig. 7, porosity of the refractory layer becomes smaller as decreasing the average particle size of the aluminium powder to be contained in the refractory material mixture. In the observation of the line B which is derived from samples containing 15 Wt% of aluminium powder, the average particle size of less than or equal to 20 µm is required for obtaining the refractory layer having a porosity less than or equal to 20%. In order to compare with this, another experimentation was performed with supplying oxygen as the combustion-assisting gas utilizing the spray coating appratus of Fig. 1. In the experimentation, propane gas was used as the fuel gas. Supply amount of propane was adjusted to supply different caloric values. e.g. 2000 kcal/kg, 3000 kcal/kg and 4000 kcal/kg. 10 Wt% of aluminium powder was contained in the refractory material mixture. As will be seen from Fig. 8, in this case, the porosity of the refractory layer formed in the experimentation could be maintained less than or equal to 20%, when the average particle size of the aluminium powder was in a range of 40 µm to 160 µm. This confirms that, in the spray coating method as proposed in the present invention, greater average particule size of metal powder can be used for performing spray coating without causing significant difference to that obtained in the conventional process utilizing substantially small Particle size of metal powder. Therefore, the present invention assures safe spray coating operation. In addition, according to the invention, since the metal particle is carried by non-combusible carrier gas, combustion of the metal powder within the refractory material supply line can be successfully prevented. Though the foregoing preferred embodiment of the spray coating apparatus of Fig. 1, employs the inert and/or non-combusible gas as carrier gas for transporting the powder state mixture of the refractory material and the metal powder, it would be possible to carry the mixture with any non-oxidizing gas. Namely, the fuel gas, such as propane gas, can be used for transporting the powder state mixture. Therefore, the device of Fig. 1 can be modified as shown in Figs. 9 and 10. In a modification of Fig. 9, the ejector feeder assembly 18 is connected to a fuel gas source 36 via a fuel gas supply control valve 80. The non-combusible gas source 20 is connected to the internal space of the hopper 28 via the non-combusible gas flow control valve 82. The fuel gas supply control valve 80 and the non-combusible gas flow control valve 82 are respectively associated with valve actuators 84 and 86 which are, in turn, connected to the control 70. Other construction of the modification of Fig. 9 is identical to that illustrated in Fig. 1. Therefore, the disclosure for respective feature in the common construction is neglected in order to keep the recitation concise enough to avoid unnecessary confusion. In the shown construction, the non-combustible gas is introduced from the non-combustible gas source into the hopper 28 to pressurize the mixture of the refractory material and the metal powder in the hopper 28. On the other hand, the fuel gas is supplied to the ejector feeder assembly 18 from the fuel gas source 36 for drawing the mixture in the hopper to the refractory material supply line 16. By introducing the mixture in the refractory material supply line 16, a combusible mixture of the refractory material, the metal powder and the fuel gas is established. Therefore, the refractory material and the metal powder are carried by the fuel gas flow to the inner nozzle 12 of the lance 10. On the other hand, in another modification in Fig. 10, the fuel gas source 36 is connected to the hopper via the fuel gas supply control valve 80. Therefore, in this arrangement, the combusible mixture is established in the hopper 28 and forced to flow through the refractory material supply line 16 by the pressure in the hopper. In this case, a branch passage 90 as shown by phantom line is provided for connecting the refractory material supply line 16 and the fuel gas source 36 via three-way valve 92 so that combustioning frame of solely the fuel gas can be established for moderately warming-up and cooling-off the surface to be treated before and after spray coating operation. With the foregoing construction, the three-way valve may connect the fuel gas source to the refractory material supply line via the branch passage while the spray coating is not performed so that the fuel gas can be directly supplied to the inner nozzle. On the other hand, when spray coating is to be performed, the valve position of the three-way valve may be switched to connect the fuel gas source to the hopper. Furthermore, so that the fuel gas in the appratus can be safely removed when the refractory material and/or metal powder to be used are to be changed, an inert or non-combusible gas source is connected to the fuel gas passage connecting the fuel gas source and the hopper, as illustrated by the phantom line in Fig. 10. In this case, a three-way valve 94 may also be provided for selectively connecting the hopper to the fuel gas source and the non-combusible gas source 20. It should be appreciated that, in both modifications set forth above, it is essential to use a fuel gas which does not contain oxygen so as to avoid danger of accidental combustion of the metal powder. While the present invention has been disclosed in terms of the preferred embodiment in order to facilitate better understanding of the invention, it should be appreciated that the invention can be embodied in various ways without departing from the principle of the invention. Therefore, the invention should be understood to include all possible embodiments and modifications to the shown embodiments which can be embodied without departing from the principle of the invention set out in the appended claims.

Claims: A method of spray coating of a refractory material onto a refractory construction, comprising the steps of: preparing a mixture of a refractory material and fine particles of powder state combustible metal; supplying said mixture with a non-oxidizing gas to discharge through a first nozzle toward the surface of said refractory construction on which a refractory layer is to be formed; supplying a fuel gas to said first nozzle so that said fuel gas is discharged with said mixture toward said surface; establishing a combustion flame by combusting said fuel gas and said combustible metal for forming refractory oxide of said combustible metal; and supplying a combustion-assisting gas via a second nozzle which is arranged adjacent said first nozzle to discharge said combustion-assisting gas around said combustion flame for assisting combustion of said fuel gas and said combustible metal. A method for spray coating as set forth in claim 1, wherein said mixture contains combustible metal powder having an average particle size greater than or equal to 50 µm. A method for spray coating as set forth in claim 2, wherein said mixture contains combustible metal powder having an average particle size in a range of greater than or equal to 50 µm and smaller than equal to 160 µm. A method for spray coating as set forth in claim 3, wherein said mixture contains combustible metal powder having an average particle size in a range of greater than or equal to 70 µm and smaller than equal to 140 µm. A method for spray coating as set forth in claim 4, wherein said metal powder is selected among aluminium, metallic silicon and combination thereof. A method for spray coating as set forth in claim 4, wherein said metal powder is selected among Al, Si, Mg, Mn, FeMn, SiMn, CaSi, FeSi, FeCr, CaC₂ and combination of two or more of the above. A method for spray coating as set forth in claim 4 , wherein said refractory material is selected among silica, alumina, mullite, chamotte, zircon, zirconia, magnesia, magnesite-chrome and combination of two or more of the above. A method for spray coating as set forth in claim 4, wherein said metal powder is mixed with said refractory material in a rate greater than or equal to 10% by weight. A method for spray coating as set forth in claim 4, wherein said metal powder is mixed with said refractory material in a rate less than or equal to 30% by weight. A method for spray coating as set forth in claim 4, wherein said metal powder is mixed with said refractory material in arrange greater than or equal to 10% by weight and less than or equal to 30% by weight. A method for spray coating as set forth in claim 2, wherein said metal powder is mixed with said refractory material in a range greater than or equal to 13% by weight and less than or equal to 20% by weight. A method for spray coating as set forth in claim 4, wherein said combustion-assisting gas is supplied in a rate at least three-times greater than the equivalent amount to the amount of the metal powder. A method for spray coating as set forth in claim 12, wherein said combustion-assisting gas is supplied in a range of supply rate greater than or equal to three-times and smaller than or equal to fifteen-times of the equivalent amount to the amount of said metal powder. A method for spray coating as set forth in claim 4, wherein in said step of supplying said fuel gas, the amount of said fuel gas to be supplied is in a rate for generating less than or equal to 5000 kcal per 1 kg of refractory material. A method for spray coating as set forth in claim 14, wherein the preferred supply rate of said fuel gas by said second means is to generate caloric value in a range of 2000 kcal to 4000 kcal. A method for spray coating as set forth in claim 1, further comprising the steps of defining a first path establishing communication between said first nozzle and a source of said mixture for supplying said mixture to said first nozzle, and providing a non-combustible gas source connected to said first path for supplying a pressurized non-combustible gas as carrier gas for carrying said mixture. A method for spray coating as set forth in claim 1, further comprising the steps of defining a first path establishing communication between said first nozzle with a source of said mixture for supplying said mixture to said first nozzle, and introducing said fuel gas into said first path at a position upstream of introduction of said mixture for supplying said fuel gas to said first path for carrying said mixture to said first nozzle. A method for spray coating as set forth in claim 17, wherein said fuel gas is a non-oxidizing fuel gas. A method for spray coating as set forth in claim 1, which further comprises the step of establishing combustion flame by combustion of said fuel gas in advance of supplying said mixture for pre-heating said surface of said refractory construction. A method for spray coating as set forth in claim 19, further comprising the step of maintaining flame by combustion of said fuel gas for a given period after terminating supply of said mixture and gradually reducing the fuel gas amount in order to gradually cool-off the surface of said refractory construction. A device for carrying out the method of any of claims 1 to 20 wherein a powder state refractory material and a powder state combustible metal having a particle size is supplied to a lance having a plurality of nozzles for discharging said refractory material and said combustible metal toward a surface on which a refractory layer is to be formed, characterized by: first means for supplying a mixture of said powder state refractory material and said powder state combustible metal with a non-oxidizing gas to a first nozzle (12) for injection through said first nozzle toward said surface (11) second means for supplying a fuel gas to said mixture upstream of said first nozzle for injection together with said mixture and; third means for supplying a combustion-assisting gas through a second nozzle (14) for supplying oxygen necessary for combustion of said fuel gas and said combustible metal. A device as set forth in claim 21, wherein said first and second nozzles are arranged concentrically. A device as set forth in claim 22, wherein said concentrically arranged first and second nozzles are surrounded by fourth means for circulating a coolant. A device as set forth in claim 23, wherein said coolant is supplied do said fourth means from a portion remote from said first and second nozzles. A device as set forth in claim 21, wherein said first means includes means for defining a first path establishing communication between said inner nozzle with a source of said mixture for supplying said mixture to said first nozzle, and said first means further comprises a non-combustible gas source connected to said first path for supplying a pressurized non-combustible gas as carrier gas for carrying said mixture. A device as set forth in claim 39, wherein said second means is connected to an intermediate section of said first path for introducing said fuel gas into the flow of said non-combusible gas and said mixture in said first path. A device as set forth in claim 21, wherein said first means includes means for defining a first path establishing communication between said inner nozzle with a source of said mixture for supplying said mixture to said first nozzle, and said second means is connected to said first path at a position upstream of introduction of said mixture for supplying said fuel gas to said first path for carrying said mixture to said first nozzle. A device as set forth in claim 21, which further comprises fifth means for controlling operation of said first , second and third means, said fifth means operating said second and third means in advance of operating said first means for establishing combustion flame for pre-heating said surface of said refractory construction. A device as set forth in claim 43, wherein said fifth means operates said first means to inoperative position to stop supply of said mixture at the end of spray coating operation and maintains said second and third means for a given period after terminating spray coating with gradually reducing the fuel gas amount in order to gradually cool-off the surface of said refractory construction.

Inventors: FUJII, TETSUYA C/O TECHNICAL RESEARCH DIVISION, MOTOYASU YAJI C/O CHIBA WORKS, NAKAMOTO, TSUYOSHI C/O CHIBA WORKS, NANBA, AKIHIKO C/O TECHNICAL RESEARCH DIVISION, NOZAKI, TSUTOMU C/O TECHNICAL RESEARCH DIVISION, SAITO, MITSUO C/O TECHNICAL RESEARCH DIVISION, WATANABE, SEIJI C/O TECHNICAL RESEARCH DIVISION
Applicants: KAWASAKI STEEL CORPORATION
Application year: 1987
Main classification: F27D1
IPC codes: F27D19, C04B35, C04B41, F27D1