Patent Document

BACKGROUND OF THE INVENTION 
       [0001]    This invention relates in general to flame spray apparatus and to methods of deposition of coatings and bulk materials with thermal spray techniques. More specifically, the invention relates to high-velocity oxidizer-fuel spraying apparatus and methods. 
         [0002]    Thermal spraying is widely used to apply metals and ceramics in a form of coating or bulk materials on different types of substrates. A majority of thermal spray methods utilize energy of hot gaseous jets to heat and accelerate particles of spraying material. When impinging the substrate, the particles form a coating. 
         [0003]    High-Velocity Oxygen-Fuel (HVOF) spraying apparatus and techniques, which use oxygen as an oxidizer gas, or High-Velocity Air-Fuel (HVAF) spraying apparatus and techniques, which use air as an oxidizer gas, generate a jet of hot gases due to combustion of a fuel and oxidizer in an internal burner at elevated pressure, usually several bars. The fuel can be gaseous (e.g., propane, methane, propylene, MAPP gas (i.e., liquefied petroleum gas (LPG) mixed with methylacetylene-propadiene), hydrogen, etc.) or liquefied fuel (e.g., kerosene). From the burner, the gas expands into an exhaust nozzle, reaching sonic velocity if the nozzle is straight. If the nozzle is convergent-divergent, further expansion into wider section of the nozzle results in formation of a supersonic velocity jet. This allows entrained particles of sprayed material to reach higher velocities and form coatings with better mechanical properties, compared to those achieved with straight nozzles. 
         [0004]    In spite of the technological advantages of higher particle velocities generated by supersonic convergent-divergent nozzles, there are some disadvantages caused by gaseous flow temperature drop in the divergent portion of the nozzle due to gas expansion. For typical industrial HVOF torches, where combustion chamber temperature typically reaches about 2600° C., the exit gas temperature is only about 1900° C. at stagnation pressures 7-8 bar. So, lowered heating capacity of a supersonic gas flow further reduces particle temperature that, in turn, leads to lower deposition efficiency (DE) of sprayed material, compromises coating quality, and applies limitations for spraying materials with high melting points. This cooling effect of expanded gas flow is even more detrimental for HVAF torches, since maximal temperature of combustion of air-fuel mixture in a combustion chamber is only about 1900° C., and exit gas temperature is about 1200° C. for typical stagnation pressure 6-7 bar, e.g. Mach numbers around 2. This temperature is lower than melting points of most commercial hard facing alloys and cermets, such as the most popular tungsten carbide (WC) based and chrome carbide (Cr 3 C 2 ) based composite powders. So, the use of convergent-divergent nozzles with HVAF torches significantly compromises coating quality and lowers DE of such materials due to lack of heat, in spite of higher particle velocities achievable with supersonic nozzles. For this reason supersonic nozzles have not found use for HVAF torches so far. 
         [0005]    Another disadvantage of a convergent-divergent nozzle is the difficulty of powder injection. For example, the powder cannot be fed axially through the combustion chamber, since being heated and partially melted in the burner it would plug the nozzle at the throat, where the cross sectional area is minimal and powder particles come in physical contact with nozzle bore walls. Though clogging can be prevented by significant increase of nozzle bore diameter, this would simultaneously increase flows of both oxidizer and fuel, which reduces economical effectiveness of the process. So, in practice, the radial powder injection into divergent part of the nozzle is usually used. However, this type of powder injection also causes problems, such as lack of heat available for particle heating in the divergent portion of a nozzle, and nozzle clogging caused by radially injected powder. 
         [0006]    Advancement in the HVAF apparatus and technique included a secondary fuel flow, which is added to an oxidizing flame jet in the divergent part of a nozzle such that any free oxygen within the flame jet is consumed by the secondary fuel to increase the static temperature of the jet in the divergent part of the nozzle. In order to combust effectively in the relatively cold supersonic jet, where fuel contact time with oxygen is too short, a very reactive secondary fuel of high flame temperature is used. The secondary fuel may be selected from the class consisting of acetylene, methylacetylene and its compounds, and hydrogen. 
         [0007]    Disadvantage of said technique and apparatus is the complexity of the process due to the need in highly reactive high flame temperature secondary fuel, different from primary fuel. At the same time there is still a problem with injection of powder axially due to the plugging of the nozzle throat. 
       SUMMARY OF THE INVENTION 
       [0008]    The present invention is related to a method of forming a coating by depositing a material onto a substrate with high-velocity thermal spray apparatus, wherein the apparatus comprises a mixing unit, a combustion chamber, and a non-clogging supersonic accelerating nozzle. The method comprises the steps of mixing of an oxidizer gas and a gaseous fuel in the mixing unit, igniting and combusting the oxidizer and gaseous fuel mixture in the combustion chamber, feeding products of combustion to the accelerating nozzle, introducing selected spraying material into accelerating nozzle to form a supersonic stream of hot combustion product gases with entrained particles of spray material, and spraying at high velocity onto a surface positioned in the path of the stream at the discharge end of the nozzle. The method further includes a step of forming a non-clogging convergent-divergent gas dynamic virtual nozzle (GDVN) in the accelerating nozzle by annularly introducing a coaxial gas flow, through a narrow continuous slot of circumferential ring geometry in the vicinity of the entrance to the diverging outlet bore of the accelerating nozzle. Thus, the hot combustion product gases discharged from a combustion chamber are compressed in diameter through gas dynamic forces exerted by a coaxially co-flowing gas, obviating the need for a solid nozzle to form a convergent-divergent flow and thereby alleviating the clogging problems that plague conventional solid nozzle, especially in its minimal diameter that creates choked flow condition needed to form a supersonic gas flow in the divergent part of the nozzle. Of particular advantage is the use of compressed air or air-fuel mixture for creating a coaxial gas flow. 
     
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         [0009]      FIG. 1  is a preferred embodiment of the invention that is a longitudinal sectional view of an internal burner of HVAF apparatus or device used to project with supersonic velocity a flow of fusible particles to build up a coating of such heat-softened and molten particles on a surface downstream of the discharge end of the apparatus illustrated. 
           [0010]      FIG. 2  is the preferred embodiment, showing an enlarged, sectional view of a throat portion of the supersonic GDVN of the apparatus of  FIG. 1  illustrating the nature of forming a supersonic GDVN by annularly introducing a coaxial gas flow through a narrow continuous slot of circumferential ring geometry. 
           [0011]      FIG. 3  is another embodiment, showing an enlarged, sectional view of a throat portion of the supersonic GDVN of the apparatus of  FIG. 1  illustrating the nature of forming a supersonic GDVN by annularly introducing a coaxial gas flow through a circular series of closely spaced nozzle orifices. 
           [0012]      FIG. 4  is yet another embodiment, showing an enlarged, sectional view of a throat portion of the supersonic GDVN of the apparatus of  FIG. 1  illustrating the nature of forming a supersonic GDVN by annularly introducing a coaxial gas flow through a permeable portion of the nozzle wall of circumferential ring geometry. 
       
    
    
     DESCRIPTION OF THE PREFERRED EMBODIMENT 
       [0013]    Referring to the drawing, a better understanding of the principles of this invention may be gauged by inspection of  FIG. 1 . In  FIG. 1  an improved internal burner type supersonic velocity flame jet apparatus indicated generally at  25  takes the form of an internal burner  26  comprised of cylindrical section  6 , which is closed off at its upstream end by a permeable burner block  12  and closed off at its downstream end by an exit accelerating nozzle piece  1 , thus forming a combustion chamber  27  internally of burner  26 . The accelerating nozzle piece  1  is provided with an axial nozzle bore, comprising an inlet bore  5  followed by an outlet diverging bore  2  that opens downstream. The radial dimension of an inlet bore  5  should be big enough in order to prevent heated powder stream  29  from touching the walls of the inlet bore  5 . The inlet bore  5 , which can be converging as shown in  FIG. 1 , diverging (not shown), or straight (not shown), or be of variable geometry (not shown), of the accelerating nozzle piece  1  is connected to the combustion chamber  27  by a converging inlet passage  4 . The rear piece  15  is provided with holes  18  and  19 , which open to the interior of the mixing chamber  23 , and which receive respectively the ends of primary oxidizer supply tube  17  and primary fuel supply tube  20 . A combustible mixture distributor  14  has a circular series of orifices  16 , which connect a mixing chamber  23  with circular shape distribution chamber  24 . A permeable burner block  12  typically made of high temperature ceramic has a plurality of small diameter orifices  13 , which open into the combustion chamber  27 . An orifice of axial powder injector  22  opens to the interior of the combustion chamber  27 , and receives the end of powder supply tube  21 . A narrow continuous slot  11  of a circumferential ring geometry shown in  FIG. 2 , or alternatively a circular series of closely spaced orifices  11   a  shown in  FIG. 3 , or alternatively a permeable portion of the nozzle wall  11   b  of a circumferential ring geometry shown in  FIG. 4  open to the interior of the accelerating nozzle  1  in the vicinity of the entrance  3  to the diverging outlet bore of the accelerating nozzle  1 , and to the interior of a circular cavity  10 . The accelerating nozzle piece  1  is provided with a hole  9  which opens to the interior of the circular cavity  10 , and which receives the end of secondary gas supply tube  8 . 
         [0014]    Thus, reactants including a fuel as indicated by arrow F 1  and an oxidizer as indicated by arrow P 1  are fed into the mixing chamber  23  where they form a combustible mixture, which is fed through the orifices  16  into the distribution chamber  24  and further, through the plurality of orifices  13  in the permeable burner block  12 , into the combustion chamber  27  with ignition and combustion taking place within the chamber  27  and hot combustion product gases pass through the accelerating nozzle piece  1 . The ignition means is not shown, but it is usually a regular spark plug placed in the combustion chamber. High melting point particles indicated schematically by arrow G may be introduced axially into burning gases within combustion chamber  27  through the tube  21  and powder injector  22  and further accelerated in the supersonic GDVN  31  formed within the bore of accelerating nozzle piece  1 . A heated powder stream  29  forms a coating  32  upon impact against a substrate  33 . 
         [0015]    In one aspect the present invention is directed to a method and apparatus for eliminating clogging of the throat of a supersonic nozzle by utilizing GDVN instead of actual solid convergent-divergent nozzle. A coaxial gas flow as indicated by arrow P 2  is fed into the circular cavity  10  through the secondary gas supply tube  8  and orifice  9 . A supersonic GDVN  31  is defined as an inner boundary of a coaxially co-flowing gas  30  through a narrow continuous slot of circumferential ring geometry  11  under pressure that is higher than the static pressure in the main flow of hot combustion product gases H. Formed this way GDVN  31  has a supersonic convergent-divergent shape having convergent  31   a  and divergent  31   b  portions, with a virtual throat  28  having flow area at sonic point A*, and exit  37  having exit flow area A. The ratio A/A* is determined by Mach number at which the spray torch is supposed to operate, and can be adjusted by changing the flow rate of a coaxial gas flow  30  forming GDVN. Thus, the main high velocity stream of hot combustion product gases, as indicated by arrows H, discharged from the combustion chamber  27  and flowing through the inlet bore  5  is further compressed in diameter through gas dynamic forces exerted by gas  30  coaxially co-flowing through a narrow continuous slot of circumferential ring geometry  11  and forming convergent portion  31   a  of GDVN  31 . The main high velocity hot gas stream H with entrained powder particles is further accelerated to supersonic velocity in the divergent portion  31   b  of GDVN  31  forming a supersonic flame jet indicated generally at  36 , characterized by oblique shock waves  7 , Mach disks  34 , and expansion fans  35 . Therefore, a supersonic GDVN  31  obviates the need for a solid nozzle to form a convergent-divergent flow and at the same time alleviates a possible build-up  38 , as shown in  FIG. 2 , which would plague conventional solid nozzle of thermal spray apparatus, if it had the same throat diameter as GDVN throat  28 . Since virtual throat  28 &#39;s cross sectional area A*, which actually forms a choke condition for the stream of hot combustion product gases H, is intentionally designed to be much smaller than any cross sectional area of the accelerating nozzle piece  1 , including entrance  3  to the diverging outlet bore of the solid accelerating nozzle piece  1 , the inlet bore  5  may have any shape, since it does not affect operation of the GDVN, e.g. it can be straight cylindrical, or diverging, or be of variable geometry, if desired or otherwise necessary. While any gas may be used for forming a coaxial gas flow that forms a supersonic GDVN, of particular advantage is the use of compressed air, which allows for significant reduction of cost of coating application. 
         [0016]    In another aspect the present invention is directed to a method and apparatus for increasing the jet temperature by adding a reactive fuel to the gases in the coaxial gas flow  30  forming a supersonic GDVN  31 . The secondary fuel as indicated by arrow F 2  may be pre-mixed with air, oxygen or other gas forming a coaxial gas flow  30  and a supersonic GDVN  31 , and fed through tube  8  and hole  9 . Alternatively, the secondary fuel may be fed at least through one additional circular series of orifices (not shown), or narrow continuous slot of circumferential ring geometry (not shown), or a permeable portion of the nozzle wall of circumferential ring geometry (not shown), located in the vicinity of the narrow continuous slot of circumferential ring geometry  11 . The secondary fuel may be low reactive gaseous fuel, selected from the group consisting of propane, propylene, methane, ethane, butane, or liquid fuel which may in the form of mist, vapor, or liquid. The secondary fuel is pre-heated by the stream of hot combustion product gases discharged from the combustion chamber  27 , reaching auto ignition temperature, and burns in the divergent portion of the coaxial gas flow  30  that forms a supersonic GDVN  31 . This burning gas expands inwards the core of the stream of hot combustion product gases, which is supersonic due to expansion in a supersonic GDVN  31 , until essentially complete mixing takes place. Therefore, the combustion of the secondary fuel increases the static temperature of a supersonic flow, which in turn increases velocity of main stream of hot combustion product gases, as well as temperature and velocity of entrained particles. Greater particle velocity and temperature are of extreme importance for low combustion temperature HVAF thermal spray process, and allow to significantly improve coating quality. When even higher particle temperature is needed, the secondary fuel may be a highly reactive gaseous fuel, selected from the group consisting of methyl-acetylene and its compounds, and hydrogen. 
         [0017]    In accordance with an exemplary embodiment, a coating is sprayed with an HVAF apparatus  25  comprising an accelerating nozzle piece  1  with means of forming a supersonic GDVN  31  (as described with reference to the  FIG. 1 ). The apparatus  25  is operated with primary air flow of about 55 liters per second, an inlet pressure of about 6.2 bar, and a primary propane flow of about 2.0 liters per second under the pressure of about 5.1 bar. The coaxial air flow  30 , forming a supersonic GDVN  31 , is about 32 liters per second, at an inlet pressure of about 6.8 bar, and a secondary propane flow is about 1.6 liters per second, at an inlet pressure of about 5.5 bar. Thus, the total heat energy generated by apparatus is about 1,140,000 Btu/hr. A coating is applied using 5-30 μm particle size tungsten carbide-cobalt-chrome 86% WC-10% Co-4% Cr agglomerated-sintered powder. The mean hardness of the coating is measured at about 1,390 HV300. Under these operating parameters, the apparatus is able to operate for a long time without nozzle plugging, generating a very narrow and focused powder stream. The particle velocity of about 1,198 m/sec and particle temperature of about 1,750° C. have been measured with AccuraSpray sensor by Tecnar Automation Ltée (Canada). 
         [0018]    Alternatively, for comparison, a regular HVAF apparatus, without supersonic GDVN, but instead having regular straight accelerating nozzle of the same length, and diameter similar to the diameter of the throat  3  of the apparatus with supersonic GDVN, was used to apply a coating with the same material: 5-30 μm particle size tungsten carbide-cobalt-chrome 86% WC-10% Co-4% Cr agglomerated-sintered powder. The apparatus operates with air flow of about 85 liters per second, an inlet pressure of about 6.3 bar, and propane flow of about 3.4 liters per second under a pressure of about 5.3 bar, thus generating 1,050,00 Btu/hr, e.g. the same total amount of heat energy as apparatus with supersonic GDVN according to the exemplary embodiment. The mean coating hardness is measured at about 1,040 HV300. The particle velocity of about 664 msec and particle temperature of about 1,690° C. have been measured with AccuraSpray sensor. 
         [0019]    Thus, the use of supersonic GDVN combined with feeding of secondary fuel to the coaxial gas flow forming supersonic GDVN, provides non-clogging operation of HVAF or HVOF apparatus, and when compared to typical HVAF apparatus with a straight cylindrical nozzle, allows for a nearly 2 fold increase in the particle velocity without lowering particle temperature, which significantly improves coating properties. 
         [0020]    In accordance with the provisions of the patent statutes, the principle and mode of operation of this invention have been explained and illustrated in its preferred embodiment. However, it must be understood that this invention may be practiced otherwise than as specifically explained and illustrated without departing from its spirit or scope.

Technology Category: 8