Dry ice blasting is a blasting technique that is comparable to sandblasting or high-pressure water blasting, but it makes use of, inter alia, solid CO2 pellets, also known as “dry ice pellets”, powder or flakes as the pellets. The great difference from the other blasting techniques is twofold. On the one hand, the pellets are very cold (−78° C.), with the result that the contamination layer suddenly cools down and shrinks. This means that this layer comes away easily from the substrate. On the other hand, the CO2 pellets sublime after they have touched the surface, which means that no additional waste is generated. This is directly one of the greatest advantages of dry ice blasting.
A device for particle blasting according to this invention and as illustrated in
The mixing device as illustrated in
As illustrated in
The sealing plate (9), illustrated, inter alia, in
A dividing wall (8) is provided between both the right supply channel (6a) and the right discharge channel (7a) and the left supply channel (6b) and the left discharge channel (7b). The dividing walls (8) ensure that the carrier gas flow will be deflected in the direction of the rotatable distribution disc (1) situated below. The dividing wall can close off the passage between supply channel and discharge channel either fully or only partially. In the latter case, part of the carrier gas will flow directly from supply channel to discharge channel, resulting in a reduced pulsating or jolting effect of the carrier gas to the gun.
The mixing plate (3) has at least one filling aperture (14), preferably having two, which connect to the second supply means. The particles from the feed hopper (13) fall through the filling apertures (14) and the first apertures (10) into the cavities (2) of the rotatable distribution disc (1). The filling of the cavities (2) can be aided by a rotatable knife (17) mounted on the upper side of the mixing plate (3). The cavities (2) remain filled with particles until they pass below a second aperture (11). At that moment the cavities (2) form part of the carrier gas flow path, and the particles that are present in the cavities (2) are entrained with the carrier gas and sent to the discharge channel (7). The mixture of particles/carrier gas then leaves the mixing device through the fourth aperture (16). In order to project the mixture towards the surface to be treated, a gun is connected by means of a hose or tube to said fourth aperture (16). By providing two fourth apertures, it is also possible to connect two guns to the mixing device.
Before the cavities (2) pass along the filling aperture and are filled again, they first pass along a venting channel (18). As illustrated in
The mixing device is designed in such a way that the particles undergo a minimal collision before the particles go into the discharge channel (7). This is achieved by making the second apertures (11) sufficiently large and providing a smooth discharge channel (7). This contrasts with the known systems, which are provided with apertures or openings on their outer circumference. In the case of such systems the particles, before being sent to the discharge channel, will first pass into a larger chamber, where a certain turbulence is present.
The rotatable distribution disc (1) (see, for example,
The rotatable distribution disc (1) comprises a first series and a second series of cavities (and possibly a third series of cavities), the said series of cavities (2) being placed at a first and second distance (and third distance) respectively from the centre point of the disc (1). If the first and second series of cavities are in an offset position relative to each other, this results in even more uniform mixing of the particles with the carrier gas.
The diameter of the distribution disc (1) and the dimensions of the cavities (2) are selected in such a way that, on the one hand, the friction between distribution disc (1) and sealing plate (9) is kept limited and that, on the other hand, sufficient particles can be mixed with the carrier gas without the speed of rotation becoming so high that the cavities would be only partially filled. Typical speeds of rotation lie in the order of magnitude of 5 to 100 rpm.
In the case of devices working with two filling apertures (14) and two second apertures (11) that connect to both the supply channel (6) and the discharge channel (7), the cavities will be emptied at the first second aperture by a gas flow flowing according to the direction of rotation of the rotatable distribution disc (1), while in the second, second aperture the cavities are emptied by a gas flow flowing in a direction opposite to the direction of rotation of the distribution disc (1). This prevents any build-up of dry ice in the cavities (2).
Where, as shown in
The device according to the invention is designed in such a way that all moving parts are disposed symmetrically relative to the rotating shaft, and that the pressure with which the seal is produced is in line with the moving shaft. As a result of the symmetrical positioning of both inlets and outlets, no moment of force is generated relative to the rotating shaft. The advantage of this symmetrical design is uniform wear of the rotatable distribution disc (1) and mixing plate (3), and also a great reduction in the wear of these parts. This results in a consistent seal during the service life. Although this is less good for the balance, force and pulsations of the particles, this device also relates to a device with one filling aperture (14), one supply channel (6), one discharge channel (7) and one second aperture (11).
The device according to the invention is designed in such a way that assembly and disassembly are very easy.
In order to have minimal leakage losses of carrier gas when the blow pressure (pressure of the carrier gas) is increased, and in order to limit the friction and use of the distribution disc (1) when the blow pressure is reduced, the seal is preferably made dependent upon the pressure of the carrier gas. In the known mixing devices the pressure-dependent seal is achieved directly at the interface with the rotor (1) and is consequently exposed to very low temperatures as a result of the dry ice. This has the disadvantage that the different components needed to achieve the seal have to meet specific requirements.
In the device according to the invention the pressure-dependent seal is achieved outside the mixing device, and consequently outside the cold zone, with the result that there is no need for specific material. This is achieved as follows: The rotatable distribution disc (1) is mounted on a rotating shaft (19), which is fitted through the hollow shaft of the reductor (21), which is driven by a motor (20). Below the reductor (21), the hollow shaft is supported by a piston (22), which receives counterpressure from a pressure chamber (23) situated on the bottom of the device. The bearing (24) provided on the upper side of the piston (22) prevents the piston (22) and the pressure chamber from rotating. This results in a very simple arrangement. Since the pressure of the pressure chamber (23) is proportional to the blow pressure, a pressure-dependent seal is achieved.
In order to make the pressure of the pressure chamber (23) proportional to the blow pressure, it is obvious to regulate the pressure circuit of the pressure chamber by means of the same pressure valve as that of the blow pressure. Notwithstanding that, this invention also comprises a system wherein the pressure in the pressure chamber (23) is regulated by means of a separate pressure valve. The present invention also relates to systems wherein the sealing pressure is not regulated by means of a pressure chamber, but by means of springs or other means making it possible to achieve a certain pressure between mixing plate (3) and distribution disc (1).
In addition, the rotatable distribution disc (1) is mounted on the hollow shaft in such a way that the connection is not rigid, which makes it possible to accommodate minor alignment differences.
Number | Date | Country | Kind |
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2006/0390 | Jul 2006 | BE | national |