TWO-FLUID NOZZLE

Abstract: The present invention is directed to a two-fluid nozzle, wherein the top face outer wall portion of a nozzle tip for forming the discharge opening is formed so that the axial direction section which is gradually smaller in diameter towards, the vertex of the center becomes circular in shape, and also, the cylindrical outer peripheral side wall portion is connected adjacent to the top face outer wall portion, a slitting split is effected by the constant width across the outer peripheral side wall portion from the vertex of the top face outer wall portion so as to form a constant wide of discharge opening across the opposite outer peripheral portions from the center of the top face portion.

Description: The present invention generally relates to a two-fluid nozzle as set out in the preambles of claims 1 and 3, and more particularly, to a highly efficient two-fluid nozzle, which is adapted to effect a wide-angle, fan-shaped atomization by a gas, liquid mixing system used in cooling high-temperature objects, etc., and especially, which is adapted to effect the atomization uniform in drop diameter, liquid amount and air amount across the entire spray pattern region, and also, does not cause cloggings, etc. Conventionally, there has been provided such a nozzle as shown in, for example, Fig. 10 as this type of two-fluid nozzle of capable of atomizing gas, water mixed mists across a comparatively wide range on the surfaces of an object. The nozzle is composed of a nozzle body 3 with a liquid flow inlet 1 and a gas flow inlet 2 formed in it, a nozzle for liquid use 4, a nozzle for gas use 5, a retainer ring 6 to be mounted in the nozzle body 3 with the nozzle for liquid use 4 and the nozzle for gas use 5 being engaged with, and a rubber-made O ring 7 interposed between the nozzle body 3 and the nozzle for liquid use 4. In the nozzle, the liquid is fed into the axial center portion of the nozzle through the nozzle for liquid use 4 from the nozzle body 3. The gas passes through a flow passage 8 in the outer peripheral portion of the nozzle for liquid use 4, and is introduced into the nozzle for gas use 5 through an orifice 9 formed in the nozzle for liquid use 4. The gas is mixed with the outer peripheral portion of the liquid in the gas-liquid mixing chamber 10 of the nozzle for gas use 5. The gas, water mixed mists are atomized from a discharge opening 12 slit in a circular arc shaped nozzle top face portion 11. Also, there has been provided, as a nozzle of a construction approximately similar to the above-described construction, a gas-liquid mixing nozzle which feeds the liquid into the central portion, feeds the gas into the outer peripheral portion thereof so as to mix them in the gas-liquid mixing chamber 10 near the discharge opening 12, and jets the mixture from discharge opening 12 which is the same in shape as the discharge opening 12 as shown in Fig. 11. The nozzle of the above-described construction has problems in that since the system of feeding the liquid to the axial center portion to mix the gas into the outer periphery of the liquid is provided, the atomized drops become larger in diameter at the central portion thereof, become smaller at the outer peripheral portion as shown in Fig. 12, thus resulting in unequal drop diameters, and so on. Since the orifice 9 through which the gas circulates within the nozzle is narrower, foreign materials such as dust and so on contained in the gas clog the orifice 9, which clogging is likely to cause the flow amount to decrease, and also a pressure loss is likely to be caused. Since the air jetted from the orifice 9 collides against the inner wall corner portion 5a of the nozzle for gas use 5, turbulence is caused and the foreign materials in the gas are likely to be accumulated even in the corner portion 5a. Especially, in the conventional embodiment shown in Fig. 10, the above-described defects are large, the nozzle of the above-described construction has many resistance portions in the flow passage of the liquid which cause pressure losses. The flow amount reduction of the gas, and the pressure loss causes lower negative pressure of the gas to be applied upon the jetting opening 4a of the nozzle for liquid use 4 and to lower the lifting performance of the liquid. From JP-A-59 179 259 is known a nozzle to spray a film of air and water for cooling a continuous casting machine. This nozzle shows an orifice at a circumferential inner surface of air piping for jetting water into a mixing chamber. In the central part of the mixing chamber a hole is provided through which air is fed to the mixing chamber and mixed with the water. This water air mixture then is ejected through a discharge opening in the tip of the nozzle. This known nozzle has the disadvantage that when feeding the air into the central portion of the nozzle and feeding the water into the outer peripheral portion thereof, the diameter of the water drops in the outer peripheral portion of the mixed liquid becomes larger. Therefore the drop diameter on the peripheral edge portion of the spray pattern becomes larger as shown in fig. 13. Further, since the rubber-made O ring is used, the durability is reduced and also, the number of the parts becomes more. Further, in the above-described conventional nozzle, the shape of the discharge opening 12 of the nozzle top face portion 11 is slit along a line X - X direction of the nozzle axial line as shown, so that the cut end portion 12b of the side face portion 12a is provided to become a rectilinear (flat shape) in a Y - Y direction which makes a right angle which the X-X direction and thus is, orthogonal to the side face portion 12a. The cut end portion 12b is shaped as shown, with an inconvenience that the distribution of the gas-liquid mixture becomes unequal and also, the diameter of the droplets becomes unequal. This is proved by experiments as described later in the comparison with the present invention. As for the shape of the discharge opening, a discharge opening 12′ might be slit into a V shape from the tip end position of the nozzle top face portion 11 to the face side as shown in, for example, Fig. 8 (B) (See for example, Japanese Laid-Open Patent Application Tokukaisho No. 56 -100663.) Above-described V-shaped slitting cut is inserted, with an inconvenience that the atomizing range capable of uniform distribution becomes narrower. This is proved by experiments as described later in the comparison with the present invention. Even in a nozzle provided with the discharge opening 12′, the passage of the fluid within the nozzle becomes complicated to easily accumulate the foreign materials and cause the pressure loss, and two fluids are mixed immediately before the discharge opening, with an inconveniences that the mixing is not effected sufficiently, the drop diameters do not become uniform. Accordingly, an essential object of the present invention is to provide a two-fluid nozzle which is free from the disadvantages of the above-described conventional nozzle, and which is capable of making the drop diameter, the liquid amount and the air amount equal across the wide range. Another important object of the present invention is to provide a two-layer nozzle of the above-described type which is capable of effecting a wide-ranged uniform atomizing operation. In accomplishing these and other objects the present invention, provides a two fluid nozzle according to claim 1. Also, the preferred embodiment of the present invention provides a system of feeding the gas into the axial center portion of the nozzle, and also, mixing the liquid near the feed end from the outer peripheral direction of the gas to be circulated along the axial center line within the nozzle. is used as a system of mixing the gas with the liquid within the nozzle. The present invention also provides a two-fluid nozzle, according to claim 3. In accordance with the preferred embodiments of the present invention, the shape of the discharge opening for shaping the slitting split is made circular or V in shape at the cut tip end portion so as to spread the atomization range to be uniformly distributed. Further, a system of feeding the gas along the axial center line and also, feeding the liquid into the outer peripheral portion thereof. After the gas, liquid mixed fluid mixed in the first mixing chamber has been circulated through the rectifying chamber, it is diffused in the second mixing chamber. The outer peripheral portion of the gas, liquid mixed fluid is forced to be collided against the wall face, so that the water drops large in the drop diameter in the outer peripheral portion is made smaller in diameter so as to make the drop diameter uniform. Therefore, the atomizing operation approximately uniform in the drop diameter, the air amount and the liquid amount may be effected across the wide range by the above-described operations. These and other objects and features of the present invention will become clear from the following description taken in conjunction with the preferred embodiments thereof with reference to the accompanying drawings, in which: Fig. 1 is a sectional view showing an embodiment of a two-fluid nozzle in accordance with the present invention; Fig. 2 is a front face view of a nozzle shown in Fig. 1; Fig. 3 is an explosive perspective view thereof; Fig. 4 is a schematic enlarged sectional view of the essential portions; Fig. 5 (A), (B), (C) are views each showing a slitting split shape of a discharge opening; Fig. 6 (A), (B) show pattern views each showing the results of an experiment embodiment 1, wherein the drop diameter, the liquid amount and the air amount in the spray pattern between the present invention nozzle and the conventional nozzle provided in shape with the discharge openings shown in Fig. 5; Fig. 7 is a diagram showing the results of an experiment embodiment 2, wherein the maximum drop diameters are compared with; Fig. 8 (A), (B) are views showing the shape of the discharge openings; Fig. 9 (A), (B) are pattern views showing the results of an experiment embodiment 3, wherein the expanses of the atomization of the nozzles having discharge openings shown in Fig. 8 (A), (B) are compared with; Fig. 10 is a sectional view showing the conventional embodiment; Fig. 11 is a sectional view showing the different conventional embodiment; Fig. 12 is a pattern view showing the drop diameter of a spray pattern in a nozzle in a case where the liquid is fed into the nozzle central portion, and also, the gas is fed into the outer peripheral portion of the liquid for the mixing operation; and Fig. 13 is a pattern view showing the drop diameter in a case where the gas is fed into the nozzle central portion, and also, the liquid is mixed with the outer periphery of the gas. Before the description of the present invention proceeds, it is to be noted that like parts are designated by like reference numerals throughout the accompanying drawings. Referring now to the drawings, there is shown a two-liquid nozzle according to the preferred embodiment of the present invention, which includes a nozzle main body 20, a core 21, a tip 22, a cap 23. The nozzle main body 20 is approximately cylindrical in shape, has large-diameter opening portions 25, 26 formed respectively in both the right, left end portions thereof, with the opening portions being connected with a gas feed pipe and a liquid feed pipe (not shown), has a concave portion 27 provided in the axial central portion with the top face thereof being open in the drawing, has a female screw portion 27a on the inner peripheral face of the concave portion 27 so as to screw the cap 23. A small diameter of gas inlet passage 28 which is drilled in a position under the axial core line ℓ - ℓ of the nozzle main body 20 and in parallel to the axial core line ℓ - ℓ communicates with the opening portion 25 connected with the gas feed pipe. The gas inlet passage 28 is bent onto the side of the concave portion 27 in the central portion of the nozzle main body 20 to open at the bottom face center of the concave portion, and also, the partition wall portion 29 is projected from the concave portion along the outer periphery of the opening to form an orifice 30. A small diameter of liquid inlet passage 31 which is open along the axial core line ℓ - ℓ, namely, on the upper portion side from the gas inlet passage 28, in one portion of the outer peripheral face of the concave portion 27 is drilled in the opening portion 26 to be connected with the liquid feed pipe. A core 21 is engaged within the concave portion 27, and a tip 22 is engaged with the tip end portion of the core 21. A cap 23 is screwed to the nozzle main body 20 with the cap 23 being engaged with the core 21 and the tip 22, so as to constitute the nozzle. The core 21 engaged into the concave portion 27 of the nozzle main body 20 forms a taper hole 33 to be expanded in a downwardly conical shape in the lower portion of the small diameter hole 32 drilled along the axial core from the top end. The taper hole 33 is surroundingly positioned through the provision of a gap from the partition wall portion 29. The space between the top end portion outer wall of the partition wall portion 29 and the inner wall of the taper hole 33 becomes narrow in the gap. The narrow space is to function as an orifice 43. By this construction, the gas is jetted into the central portion of the taper hole 33 from the orifice 30, and also, the liquid is jetted into the outer peripheral portion of the gas from the orifice 43 so as to feed the liquid into the outer peripheral portion of the gas to effect a mixing operation in the first mixing chamber A to be constituted in the inner portion of the taper hole 33. The small diameter hole 32 to communicate with the taper hole 33 is set comparatively long to constitute the long rectifying chamber B so as to sufficiently effect the rectifying operation of the mixing fluid to be mixed in the first mixing chamber A. A second mixing chamber C is provided in the tip 22 in adjacent contact on the tip end side of the core 21 with the hole 36 larger in diameter than the rectifying chamber B being formed on the basic end side communicating with the rectifying chamber B as shown. A top face outer wall portion 38 which becomes circular in an axial direction section that becomes gradually small in diameter towards the top end side is formed on the tip end side of the tip 22 as shown, and also, a cylindrical outer peripheral wall portion 41 is connected with the top face outer wall portion 38, and an intermediate diameter hole 39 having a circular arc shaped tip end portion is formed in the inner portion of the tip 22. The intermediate diameter hole 39 communicates with the tip end side of the large diameter hole 36 to provide a jetting chamber E, and also, a wall face 40 is formed on the outer peripheral portion of the intermediate diameter hole 39 in the communication portion between the large diameter hole 36 and the intermediate diameter hole 39. The wall face 40 is formed on the outer peripheral portion of the tip end face of the second mixing chamber C so that the fluid on the outer peripheral portion of the mixed fluid jetted from the rectifying chamber B into the second mixing chamber C is adapted to be collided against the wall face 40. D1 ≦ D2, D3 ≦ D2 are set, wherein the diameter of the rectifying chamber B is D1, the diameter of the second mixing chamber C is D2, the diameter of the jetting chamber E is D3. The fluid of the outer peripheral portion of the mixing fluid which jets into the second mixing chamber C from the rectifying chamber B by the length L of the second mixing chamber C is set to be forced to be collided against the wall face 40. The discharge opening 42 is formed, by the slitting split across the outer peripheral side wall portions 41 on both the sides from the vertex portion on the central line of the nozzle, in the circular top face wall portion 38 of the tip 22. As shown in Fig. 4, the discharge opening 42 is provided so that the vertex portion 42a and the opposite side face portions 42b, 42b are set by the same width, and the cut tip end portions 42c, 42c of the side face portions 42b, 42b are formed circular. The shape of the cut tip end portion 42c of the discharge opening 42 is not restricted to the circular arc shape, but may be formed into a cut shape of a V-shaped acute angle. The two-fluid nozzle of the above-described construction will be described in construction hereinafter. The gas (air in the present embodiment) flowed in from the gas inlet opening 25 is jetted into the first mixing chamber A from the orifice 30 in the central axial portion of the nozzle, the liquid (water in the present embodiment) flowed in from the liquid inlet opening 26 into the outer peripheral portion of the air is jetted from the orifice 43, so that the water is mixed from the outer peripheral portion of the air. Although the air and the water mixed almost collectively by the mixing operation in the first mixing chamber A, the water drops become comparatively larger in the outer peripheral portion, and become smaller in the central portion. In this condition, the mixed liquid flows into the rectifying chamber B. In the rectifying chamber B, the gas, water mixed liquid which is large in the water drop is circulated along the inner wall, the gas, water mixing liquid small in the water drop is circulated into the central portion. The gas, water mixed liquid which is jetted from the tip end of the rectifying chamber B into the second mixing chamber C of the large diameter is diffused as shown in Fig. 4, so that the mixed liquid on the outer peripheral portion mainly collides against the wall face 40 on the front face. Therefore, the water drops large in the drop diameter on the outer peripheral portion become smaller in the drop diameter, and become approximately equal in the drop diameter to the water drops in the central portion. The gas, water mixed liquid which has become equal in the drop diameter flows into the jetting chamber E of the small diameter and is jetted from the discharge opening 42. The jetted gas, water mixed mist becomes a spray pattern of a wide-angle fan shape by the shape of the discharge opening 42, and the drop diameter becomes equal, both the air amount and the liquid amount become almost equal across the whole spray pattern region as shown in the experiment embodiments to be described later. As shown in the present invention, in the gas, water mixing nozzle of a system of feeding the air into the central portion of the nozzle, and feeding the water into the outer peripheral portion thereof, it is natural that the diameter of the water drops in the outer peripheral portion of the mixed liquid becomes larger. When a means of forcing the large water drops in the outer peripheral portion to be collided against the wall faces to make the diameter thereof smaller as in the present invention is not used, the drop diameter on the peripheral edge portion of the spray pattern becomes larger as shown in Fig. 13. In the present invention, the water drops are caused to be collided against the wall faces as described hereinabove, the drops larger in diameter than the drop diameter shown in one dot chain lines in Fig. 13 are removed so that the drop diameter is made smaller. (Experiment Embodiment 1) According to the comparison experiments of the performance of the nozzle related to the above-described present invention and the performance of the nozzle shown in the above-described Fig. 12, the results were shown in Fig. 6 and Fig. 7. Namely, in the nozzle in accordance with the present invention, wherein the shape of the discharge opening 42 shown in Fig. 5 (A) was made circular in the cut tip end portion 42c, the drop diameter, the liquid amount and the air amount were uniform in the range wider than the central portion of the spray pattern. Even when the cut tip end portion 42c of the discharge opening 42 was cut into a V-shape as shown in Fig. 5 (B), the distribution was uniform across the entire region of the spray pattern approximately as shown in Fig. 6 (A). In the nozzle where the cut tip end portion 12b of the discharge opening 12 in the conventional embodiment shown in Fig. 5 (C) was bent at a right angle with respect to the side face portion, and was made into a flat shape, and also, the water was fed into the central portion of the nozzle, the air was fed into the outer peripheral portion thereof, the central portion of the spray pattern was larger in the drop diameter, the outer peripheral portion was smaller, thus resulting in unequal distribution. The liquid amount was more in the central portion, was less in the outer peripheral portion. The air amount was inversely less in the central portion, was more in the outer peripheral portion, thus resulting in unequal distributing condition. (Experiment Embodiment 2) According to the measurement of the nozzle in accordance with the present invention shown in Fig. 5 (A), (B) and of the maximum drop diameter of the nozzle in the conventional embodiment shown in Fig. 5 (C), the results were shown in Fig. 7. Namely, the drop diameter was approximately uniform across the entire region of the spray pattern in the (A), (B) of the present invention. In the conventional embodiment (C), the drop diameter in the central portion was larger, the drop diameter in the peripheral portion was smaller, thus resulting in unequal drop diameter. (Experiment Embodiment 3) The comparative experiments were effected in the slitting split shape of the nozzle discharge opening and the expanse of the atomization. Namely, as shown in Fig. 8 (A), in the case of the nozzle in accordance with the present invention, wherein it was formed with a slitting split of a given width from the circular arc shaped (in section) top face wall portion to the side face wall portion, and also, only the cut tip end portion was formed into a V-shape, the range of atomization capable of uniform distribution was wider (240 mm) as shown in Fig. 9 (A). On the other hand, as shown in Fig. 8 (B), in the nozzle provided with a discharge opening 12′ which was formed in the whole into a V-shape slitting split across the side face from the top end point, the range of the atomization capable of uniform distribution was narrower (150 mm) as shown in Fig. 9 (B). In the present embodiment, only the slitting split shape was different, with the other conditions being the same. A tip which was different in the slitting split shape was mounted on the nozzle of the above-described embodiment in accordance with the present invention. As shown in Fig. 8 (B), when the V-shaped slitting split was provided in its entirety, the uniform distribution was not available if the deeper cut was provided. When the uniform distribution was tried to be provided, the atomization range became narrower as described hereinabove. As is clear from the foregoing description, the two-fluid nozzle in accordance with the present invention has the following effects. (1) Since the shape of the discharge opening to be formed by the slitting split is provided with a constant width across the side face portion from the top face portion, and also, the cut tip end portion is made circular or V in shape, the spray pattern of the uniform distribution may be provided across the wide range. (2) In the first mixing chamber, the gas, liquid mixed fluid where the fluid is fed into the outer periphery of the gas to be fed into the central portion and is mixed is jetted into the second mixing chamber of the large diameter through the long rectifying chamber. In the second mixing chamber, the outer peripheral portion of the gas, liquid mixed fluid is adapted to be collided against the wall faces on the tip end side. Thus, the water drops of the large diameter in the outer peripheral portion is crushed into the small diameter. Thus, the drop diameter may be made uniform throughout the entire region of the spray pattern. (3) Since in the first mixing chamber adjacent to the gas inlet and the liquid inlet, the gas and the liquid are mixed, the mixed fluid is adapted to be circulated as far as the discharge opening straight along the axial center line of the nozzle, both the fluid and the gas are simple in the flow passage, so that positions for causing the cloggings and vortex flows are not provided, and the pressure loss is not caused, either. (4) The nozzle of the present invention is composed of four parts. Since the number of the parts may be reduced as compared with that of the conventional nozzle, the reduction of the cost may be effected. (5) Since the rubber-made O ring as in the conventional nozzle is not used, the considerable improvement in durability may be effected. Although the present invention has been fully described in connection with the preferred embodiments thereof with reference to the accompanying drawings, it is to be noted that various changes and modifications are apparent to those skilled in the art. Such changes and modifications are to be understood as included within the scope of the present invention as defined by the appended claims.

Claims: A two-fluid nozzle which is adapted to be fed by a gas and a liquid respectively from a gas inlet (25) and a liquid inlet (26) formed in a nozzle main body (20), to mix them within the nozzle main body and which is adapted to atomize the gas-water mixture through the discharge opening, characterized in that the top face outer wall portion (38) of a nozzle tip (22) comprising said discharge opening (42) is formed so that the axial section is gradually smaller in diameter towards the vertex of said nozzle and becomes circular in shape, and also in that the cylindrical outer peripheral side wall portion (41) of the nozzle tip is connected continuously to the top face outer wall portion (38), the discharge opening being provided as a split having a constant width (42a,b) along the outer peripheral side wall portion (41), and the in that end portions (42c) of said split are formed circular or V-shaped. A two-fluid nozzle according to the claim 1, wherein the gas to be fed the nozzle is fed into the axial center portion (30) of the nozzle, and also, the liquid is mixed near the feed end (43) from the outer peripheral direction of the gas to be circulated along the axial center line within the nozzle. A two-fluid nozzle, comprising a first mixing chamber (A) where the liquid is fed into the outer periphery (43) of the gas fed along the axial center line (1) on the basic end side of the nozzle main body (20) so as to effect the mixing operation, characterized in that a rectifying chamber (B) is in communication with the first mixing chamber (A) to bring the mixed fluid to the tip end side along the axial center line, a second mixing chamber (C) large in diameter (D₂) is provided on the tip end side of the rectifying chamber (B), a wall face (40) against which the fluid of the outer peripheral portion of the mixed fluid exhausted into the second mixing chamber (C) from the rectifying chamber (B) collides is formed on the tip en side of the second mixing chamber (C) and, an atomizing operation is effected from the discharge opening (42) through a jetting chamber (E) in communication with the tip end side of the second mixing chamber (C). A two-fluid nozzle according to claim 3, wherein the jetting chamber (E), the top face outer wall portion (38) is made of a tip (22) so that the axial section which is gradually smaller in diameter towards the vertex of the center becomes circular in shape, and also, the cylindrical outer peripheral side wall portion (41) may be connected continuously to the top face outer wall portion (38), a slitting split (42) is provided by a constant width across the outer peripheral side wall portion (41) from the vertex of the top face outer wall portion (38) so as to form a constant width of discharge opening across the opposite outer peripheral portions from the center of the top face portion, and also, the cut tip end portion (42c) of the discharge opening (42) of the opposite outer peripheral portions is formed circular or V in shape. A two-fluid nozzle according to any of the claims 1 to 4, characterized in that the rectifying chamber (B) has a small cylindrical shape of diameter (D₁), that the second mixing chamber (C) has a large cylindrical shape with a diameter (D₂) larger than that of the rectifying chamber (D₂ > D₁) and that the diameter (D₃) of the jetting chamber (E) is smaller than the diameter of the second mixing chamber (C) (D₃ < D₂).

Inventors: IKEUCHI, HIROSHI, OHNISHI, NORIO
Applicants: H. IKEUCHI & CO., LTD.
Application year: 1990
Main classification: B05B1
IPC codes: B05B7, B05B1