• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The device comprises a plurality of superimposed sectional plates each of which is provided with aligned holes defining a plurality of ducts lying in side-by-side relation, each of the ducts containing a plurality of helically twisted vanes which are angularly displaced with respect to one another at angles of substantially 90 DEG .
    公开号:SU1058491A3
    申请号:SU813338400
    申请日:1981-07-31
    公开日:1983-11-30
    发明作者:Манфре Джованни
    申请人:Чентро Ричерке Фиат С.П.А. (Фирма)；
    IPC主号:
    专利说明:

    2. The device according to claim 1, which is based on the fact that, in order to obtain a melt with a certain value of the concentration of the solid phase, it is equipped with a cooling means.
    3. The device according to claim 2, characterized in that the coolant is made in the form of a plurality of additional holes in the flat elements forming channels for the circulation of the coolant.
    4. A device according to claim 1, characterized in that the length of the spiral blades is equal to the length of the holes.
    The invention relates to a plant for the preparation of a mixture comprising a solid and a liquid phase of an alloy of a metal of the type used in the processes defined by a semi-liquid.
    It is known that in metallurgy alloys of metals have a temperature range outside which they harden, and the duration of this interval characterizes the alloy itself. Above the upper limit (liquidus) of this interval, the alloy is completely in the liquid state, while below the lower limit (solidus) the alloy is in the solid state. In the interval during which solidification occurs, two phases (liquid and solid) are distinguished. the relative amounts of which are a function of the temperature and composition of the cciMoro alloy.
    Under normal solidification conditions, the solid is in a dendritic form, i.e. in the form of tree-like structures, the characteristic feature of which is a perpendicular branch from the main branches of the secondary, tertiary, etc. branches. Once the fraction of solids reaches 20%, the dendrites present form a tree-like structure, which increases the viscosity beyond the allowable limits for the casting operation.
    Processes are known by which it is possible to prepare a mixture consisting of solid and liquid phases of a metallic material, which, despite a rather high concentration of the solid phase, has the characteristic: fluid properties, in particular, relatively low viscosity.
    During these processes, slip is caused between different particles, which are kept in motion in such a way as to destroy within certain limits the dendritic interconnections formed during solidification of the mixture, and prevent further growth of the dendrites themselves. In this case, the dendritic fragments are independent of each other and have the tendency to the adoption of spheroidal forms under the influence of continuous mechanical action.
    This slip, which can be calculated using a relative velocity gradient, can also be obtained inside the mixture using a turbulent flow and a laminar and constant fluid flow, in which, in other words, different particles of the mixture move at a predetermined speed depending on their position relative to the walls of the chamber through which they pass.
    The closest to the invention in technical essence and the achieved result is a method of preparing a mixture consisting of solid and liquid phases of an alloy of a metal, and an installation for carrying out this process.
    The device consists of a vessel in which a mixture flow is created and devices for transmission are arranged in the form of spiral blades, each of which is intended to cross-section the flow of flow along. at least two streams and giving each of them a spiraling trajectory of movement. In this setting, the mixture is subjected to sliding forces and continuous shocks, as a result of which the mixture leaving the installation has a very high percentage of solid phase, while the viscosity of the mixture itself is rather low l.
    It was found that although completely satisfactory results can be obtained at the described installation, but if the mixture should have a predetermined and not very high viscosity, for example, it is necessary to ensure its suitability for subsequent chill casting, the specified percentage of solids is not may be increased beyond a certain limit, which is not
    exceeds 60% if the dimensions of the installation are designed to obtain a fairly high flow rate of the mixture, such as, for example, for high-performance industrial installations.
    The purpose of the invention is to lower the melt viscosity and increase the percentage of solid phase in it.
    This goal is achieved by the fact that in a device for preparing a melt containing a solid and a liquid phase including a tank for a melt with a bottom and devices for dividing the melt stream, made in the form of spiral blades, the melt tank for the melt is formed by a plurality of stacked flat elements, made with through holes forming rows of vertical channels with a diameter of 2-10 mm, in each of which a longitudinal axis is placed along one longitudinal axis along a twist of a plate or ryo There is an angle of 9 relative to the lower end and divides each hole into two longitudinal chambers, while the lower end of the spiral blade of the preceding flat element is 90 ° relative to the upper end of the spiral blade of the subsequent flat element and the ratio the length of each hole to its diameter is equal to one.
    The device may be provided with a cooling means, made, for example, in the form of a plurality of additional holes in the planar elements forming channels for circulation of cooling liquid.
    The length of the spiral blades is equal to the length of the holes.
    Figure 1 shows the device, a longitudinal section; figure 2 - spirogshevidnaya blade, perspective view; Fig. 3 shows a family of curves, illustrating the behavior of the device in operation.
    The device consists of a plurality of planar elements 1f superimposed on each other in each of which there are a series of holes 2 that intersect the element itself and are located in any given configuration. Thus, when such elements are superimposed on each other like this, with one pair of contacts. surfaces, different apertures 2 define the multiplicity of channels 3 that intersect the entire stack formed by these elements.
    These overlapping elements can be delimited by any transverse plane, for example, cylindrical, and to keep them in the correct position
    to each other, mounting devices of any type can be provided, composed, for example, by pairs of cylindrical surfaces 4, which can be paired with each other (FIG. 1), or with a pin, rivet, or the like.
    The various channels 3 are connected to tank 5, in which a predetermined amount of alloy in liquid STATE can be located. It can come from a convenient melting point for these purposes. between which and the reservoir a device may be provided, which exerts pressure on the alloy, continuous or intermittent action, created, in the first case, by a gear pump and a piston pump in the second.
    The staggered elements are cooled by the corresponding cooling means of the gradual cooling of the material, which flows in channels 3, and each of them produces a predetermined temperature gradient DT / L, defined as the temperature variation τT as a function of the distance L, traversed material in the channel. For this purpose, corresponding holes 6 can be made in the elements 1, which form channels that are part of the cooling circuit. .
    To use the mixture, the lower output of the channel 3 can be connected, for example, to a mold.
    In each hole 2 of the element 1, means are provided for separating and transferring the material & la, arranged so that through them. passes the material flowing along the axis through the holes themselves. These means consist of a plurality of spiral blades 7, each of which divides, a flow of material moving under pressure to at least two independent jets 8 and 9 and causes each of them to flow along such a trajectory that in each jet formed by the subsequent blade flowed parts of both jets formed n. immediately preceding the blade.
    For this purpose, each blade can have a shape, as shown in Figure 2, i.e. can be obtained by twisting the plate around the longitudinal axis. The axial length of each blade and the pitch of this helix are chosen so that the edges of the ends, respectively, the front end 10 and the rear end 11 of each blade, B1, would be relative to each other at an angle of 90. Obviously. under these conditions, the flow of material passing through the opening 2 is divided by each blade into two essentially equal jets 8 and 9 and each of them rotates, the passage through the blade, on an angle. As seen in Fig. 1, successively The blades are rotated to each other also at an angle of 90 so that the rear edge of each of them is orthogonal to the leading edge of the subsequent blade. These blades can be constructed from any material possessing physical and chemical resistance against the alloy passing through them, for example rbida Wolff mA / cermet graphite material etc. Such blades are attached to the corresponding element 1 by any convenient method using the appropriate fastener, or they can be made as one unit with the element itself. Moreover, an installation can be constructed where the blades would alternately be arranged along the left and right helix lines. and for the purposes indicated below, the diameter of each hole 2 is relatively small and is within 210 mm, and the ratio between the axial length of the hole itself and its diameter is of the order of unity. The proposed installation operates as follows. The metal alloy, which is brought to liquid by melting, enters into the pressure vessel 5, the value of which is chosen so that the liquid can be overcome, but dynamic congestion that the material itself encounters as it passes through channel 3. This is done in order so that the material leaves, the lower edges of the holes of the channels are at a given speed. The material present at the front end of each channel and still fully liquid is gradually cooled as it passes through the channel. The material supplied to the first blade 7 of any of the channels is divided into two jets 8 and 9, which are indicated by arrows in fig. 2. With the passage of the first channel, each jet 8 and 9 rotates, mainly, under ear-noise 90 and, therefore, when it arrives. And the next blade section; there is another, two jets. From this it follows that each jet flowing through one of the two channels formed by the second blade of channel 7 is actually. It consists of a material coming in / from two jets 8 and 9 that have passed through each of the channels formed by a not directly intermediate blade. Similarly, when each of the formed jets passes the third blade, it is further divided into two jets. Finally, when the material passes through each of the blades 7, it is subdivided into two independent jets, each of which is formed by the production of material from the self-propelled jets flowing after the passage of the immediately preceding blade. At that time, as the alloy in the longitudinal direction passes through the channel .3, it is cooled due to the action of means of cooling and tends to form a mixture containing a solid and a liquid phase, in which the solid content increases as it cools, i.e. . gradually, as the material passes through the channels 3. The particles of the material belonging to the flow that forms each of the jets passing through the blade 7 begin to move at a given speed, which obviously depends on the position occupied by the jet itself relative to the surfaces separating the associated jet (the surface of the blade 7 and holes 2). As a result, as long as the mixture flows past each of the blades, it is exposed to sliding, which obviously depends on the speed of the distribution of the various flows of each jet. This slip can be calculated using a slip gradient determined by the ratio between the difference in the speed of the two streams and the distance between them. Due to this slip between different particles, which is greater, the greater the corresponding gradient, dendritic bonds, which tend to form in the mixture, are gradually destroyed as the material passes through the blade, and the emergence of new similar bonds is inhibited. As soon as the material leaves one blade and enters the next one, it is in a completely different speed range due to the fact that different particles are in flows whose position relative to the surfaces cutting off the associated flow is completely different from the position in which the flows were in the preceding part contained the same particles. In fact, b; if we assume that, for example, the flow that is located in the first blade in close proximity to the surface of the blade itself, and not in its center, and which therefore has a very low (almost zero) speed due to its proximity to this surface if this stream is fed to the next trap. jaws, it is located essentially in the center of the jet being ejected. In other words, at a slightly longer distance from the surface of the blade itself. From this, it is clear that the flow in this position has a slightly higher speed than the corresponding flow had on the previous blade. This abrupt change in the velocity that various particles undergo from going from one blade to the next leads to a significant increase in the gradient of the slip, which contributes to a significant increase in the slip and impact of particles belonging to different streams against each other, and therefore leads to on a substantial scale to the destruction of dendritic bonds, which tend to form in the solid phase material passing along each of the blades 3. While the material flow moves along each and channels 3, it is also exposed to the temperature gradient L T / L, i.e., in the difference in temperature & T with the difference in the distance L, traveled by alloy in each channel 3, which gives an idea of the cooling rate in the channel itself. By experimenting with the installations under the proposed one, with channels of 3 different diameters and working under different conditions of operation, it was found that the ratio between the viscosity fj of the mixture obtained and the concentration C of the solid phase itself can be expressed using curves as shown in FIG. 3, where each of them is related to a given temperature gradient uT / L, (or cooling rate), which remains different. The temperature gradient is a function, primarily of the diameter of the channels 3, as well as the operating conditions of the installation (cooling efficiency, alloy speed, etc.) and tends to increase with decreasing diameter. The various curves of this family, designated by the reference letters G ;, G and G.3rf, are associated with gradually decreasing temperature gradients. Obviously, from these curves, if it is necessary to obtain a mixture with a very low specified viscosity of 5 (Figure 2) and at the same time with a very high concentration of the solid phase C, then these conditions can be fulfilled only at the installation, where also get a very low temperature gradient (or cooling rate) liT / .L, equal to GI (installation on which it is possible to obtain temperature gradients Gj and G;), can give a mixture with the same viscosity 1, but only with a concentration of solid phases C and c. much smaller than SL). From the above explanations, it follows that in order to ensure optimal conditions, it is necessary to force the material to move along channels 3 with a low sliding speed. However, the installation also allows to obtain a high speed of movement of the mixture, which depends solely on the number of channels 3 (and, therefore, holes 2) provided on the overlapping elements 1, therefore, the installation according to the invention is capable of with at the same time very low viscosity and very high concentration of the solid phase and, according to its data, surpasses the already known installations in this area, and also has a high flow velocity, such installations represent It is of interest to organize the process on an industrial basis. Structurally, the installation is very simple and, with an increase or decrease in the number of overlapping elements, 1 is suitable for working with various mixtures. It is obvious that modifications and changes in the form and arrangement of the various parts of the device according to the invention can be made without deviating from the essence of the invention itself.
    权利要求:
    Claims (4)
    [1]
    1. DEVICE FOR PREPARING A MELT CONTAINING SOLID AND LIQUID PHASES, including a tank for a melt with a bottom. And devices for separating a melt stream made in the form of spiral blades, which is different from the fact that, with the aim of a decrease in the viscosity of the melt and an increase in the percentage of the solid phase in it, the bottom of the vessel for the melt is formed by a multitude of flat elements stacked in a stack; connected with through holes, forming rows of vertical channels with a diameter of 2-10 mm, in each of which along the longitudinal axis there is one spiral blade formed by twisting the plate, or ribs around the longitudinal axis with the upper end of each spiral blade at an angle of 90 ° the lower end and dividing each hole into two longitudinal chambers, while the lower end of the spiral blade of the preceding flat element is located at an angle of 90 ° relative to the upper end of the spiral blade of the last traveling flat element and the ratio of the length of each hole to its diameter is equal to unity.
    SU „„ 1058491
    [2]
    2. The device according to π. 1, the fact that, in order to obtain a melt with a certain concentration of the solid phase, it is equipped with a cooling agent.
    [3]
    3. The device pop, 2, characterized in that it is cooling; The means are made in the form of a plurality of additional holes in the flat elements forming channels for the circulation of the coolant.
    [4]
    ,4. The device according to claim 1, characterized in that the length of the spiral blades is equal to the length of the holes.
    类似技术:
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    同族专利:
    公开号 | 公开日
    GB2080692B|1985-04-03|
    GB2080692A|1982-02-10|
    DE3126849A1|1982-04-15|
    DE3126849C2|1990-01-18|
    FR2487854B1|1985-12-20|
    FR2487854A1|1982-02-05|
    US4396180A|1983-08-02|
    IT1129126B|1986-06-04|
    IT8068246D0|1980-08-01|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3773098A|1972-02-04|1973-11-20|Bjorksten J|Method of static mixing to produce metal foam|
    FR2189107B1|1972-06-19|1976-08-06|Clasen Heinrich|
    US3902544A|1974-07-10|1975-09-02|Massachusetts Inst Technology|Continuous process for forming an alloy containing non-dendritic primary solids|
    FR2311577B1|1975-05-21|1977-12-09|Exxon France|
    FR2412627B1|1977-12-22|1980-08-22|Rhone Poulenc Textile|
    IT1119287B|1979-06-20|1986-03-10|Fiat Ricerche|PROCEDURE FOR THE PREPARATION OF A MIXTURE INCLUDING A SOLID PHASE AND A LIQUID PHASE OF A METAL ALLOY AND DEVICE SUITABLE TO CARRY OUT SUCH PROCEDURE|AT31579T|1983-08-04|1988-01-15|Alusuisse|METHOD AND DEVICE FOR FEEDING METAL INTO A METAL MELT.|
    IT1229029B|1989-04-14|1991-07-12|Polvara Maria Crosti Giovanni|PROCESS FOR THE PRODUCTION OF CAST ALUMINUM ALLOYS IN THE SEMI-LIQUID STATE, AS WELL AS PLANT FOR ITS IMPLEMENTATION.|
    IT1243100B|1990-04-12|1994-05-24|Stampal Spa|PROCEDURE AND RELATED EQUIPMENT FOR INDIRECT CASTING OF BILLETS WITH METALLIC ALLOY IN THE SEMI-LIQUID OR PASTY STATE|
    SE9203842L|1992-12-21|1994-06-22|Alfa Laval Food Eng Ab|Static mixer|
    MY110990A|1993-06-03|1999-07-31|Atomaer Pty Ltd|Multiphase staged passive reactor|
    GB0323918D0|2003-10-11|2003-11-12|Kvaerner Process Systems As|Fluid phase distribution adjuster|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    IT68246/80A|IT1129126B|1980-08-01|1980-08-01|HIGH CAPACITY DEVICE FOR THE PREPARATION OF A MIXTURE INCLUDING A SOLID PHASE AND A LIQUID PHASE OF A METAL ALLOY|
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