The invention relates to a droplet break-up device, in the art also known as a drop on demand system or a continuous printing system, configured for ejecting droplets from a printing nozzle in various modes.
In this connection, by a continuous jet printing technique is meant the continuous generation of drops which can be utilized selectively for the purpose of a predetermined printing process. The supply of drops takes place continuously, in contrast to the so-called drop-on-demand technique whereby drops are generated according to the predetermined printing process.
A known device is described, for instance, in U.S. patent specification U.S. Pat. No. 5,969,733. This document discloses a so-called continuous jet printer for printing materials comprising viscous fluids. With this printer, viscous fluids can be printed. During the exit of the viscous fluid through an outlet channel, a pressure regulating mechanism provides, with a predetermined regularity, variations in the pressure of the viscous fluid adjacent the outflow opening. This leads to the occurrence of a disturbance in the fluid jet flowing out of the outflow opening. This disturbance leads to a constriction of the jet which in turn leads to a breaking up of the jet into drops. This yields a continuous flow of regressive drops with a uniform distribution of properties such as dimensions of the drops. The actuator of the regulating mechanism is provided as a vibrating plunger pin, actuated by a piezo-element. This construction is relatively expensive and difficult to upscale to multiple nozzles.
In one aspect, the invention aims to provide a break-up device that is simple in construction and can be scaled easily to multiple nozzles, to overcome the limitations of current systems.
According to an aspect of the invention, a droplet break up device is provided comprising a chamber for containing a pressurized printing liquid; an outlet channel, provided in said chamber for ejecting the printing liquid; and an actuator for breaking up a fluid jetted out of the outlet channel; wherein the actuator comprises a revolving member having a bottom surface arranged opposite the outlet channel, the bottom surface comprising a surface deformation shaped to provide a pressure pulse near the outlet channel.
According to another aspect of the invention, a method of ejecting droplets for printing purposes is provided, comprising providing a chamber for containing a printing liquid and an outlet channel in the chamber; pressurizing the liquid and imputing a pressure pulse to the liquid near the outlet channel so as to break up a fluid jetted out of the outlet channel; wherein the pressure pulse is imparted through a rotation induced jet disturbance.
Through the revolving member, a simple and effective jet disturbance can be created, which is easily scalable to multiple nozzle systems.
In addition, by virtue of high pressure, fluids may be ejected having a particularly high viscosity such as, for instance, viscous fluids having a viscosity of 300·10−3 Pa·s when being processed. In particular, the predetermined pressure may be a pressure between up to 600 bars.
Other features and advantages will be apparent from the description, in conjunction with the annexed drawings, wherein:
The droplet break up device 1, also indicated as printhead, shown schematically in
The outlet channel 4 is included in a relatively thin nozzle plate 8 which can be a plate manufactured from metal foil, of a thickness of 0.3 mm in this example. The outlet channel 4 in the plate 8 has a diameter of 50 μm in this example. A transverse dimension of the outlet channel 4 can be in the interval of 2-500 μm, more preferably in the order of 5-250 micron, even more preferably between 5-100 micron. As an indication of the size of the pressure regulating range, it may serve as an example that at an average pressure in the order of magnitude of 0.5-600 bars [≡0.5-600×105 Pa]. The printhead 1 may be further provided with a supporting plate (not shown) which supports the nozzle plate 8, so that it does not collapse under the high pressure in the chamber.
It is noted that the number of grooves 7 along a circumference directly multiply the break-up frequency, so that for example, at a rotation speed of 8000 rpm, with 400 grooves a droplet frequency of over 53 khz can be obtained. The rotation speed may be well between 500-20000 rpm and the number of grooves may be between 5 and 1000, reaching breakup frequencies well above 20 kHz.
The invention has been described on the basis of an exemplary embodiment, but is not in any way limited to this embodiment. In particular, the scope of the invention includes all forms of droplet generation, for example, for spray drying, rapid prototyping or other printing applications. Diverse variations also falling within the scope of the invention are possible. To be considered, for instance, are the provision of regulatable heating element for heating the viscous printing liquid in the channel, for instance, in a temperature range of 15-1300° C. By regulating the temperature of the fluid, the fluid can acquire a particular viscosity for the purpose of processing (printing). This makes it possible to print viscous fluids such as different kinds of plastic and also metals (such as solder).
Number | Date | Country | Kind |
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07115425 | Aug 2007 | EP | regional |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/NL2008/050578 | 9/1/2008 | WO | 00 | 3/19/2010 |
Publishing Document | Publishing Date | Country | Kind |
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WO2009/028947 | 3/5/2009 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
3709432 | Robertson | Jan 1973 | A |
3864691 | Schroeder | Feb 1975 | A |
4190844 | Taylor | Feb 1980 | A |
4341310 | Sangiovanni et al. | Jul 1982 | A |
5534904 | Sheinman | Jul 1996 | A |
5969733 | Sheinman | Oct 1999 | A |
6106107 | Sheinman | Aug 2000 | A |
6362843 | Silverbrook | Mar 2002 | B1 |
6375088 | Warrick | Apr 2002 | B1 |
20020171716 | Jeanmaire | Nov 2002 | A1 |
Number | Date | Country |
---|---|---|
0 152 200 | Aug 1985 | EP |
62 083062 | Apr 1987 | JP |
04-011961 | Jan 1992 | JP |
2000-033701 | Feb 2000 | JP |
2002-143745 | May 2002 | JP |
WO 2004011154 | Feb 2004 | WO |
WO 2004018212 | Mar 2004 | WO |
WO 2006101386 | Sep 2006 | WO |
Entry |
---|
International Search Report dated Nov. 14, 2008, for PCT/NL2008/050578. |
Number | Date | Country | |
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20100201758 A1 | Aug 2010 | US |