Thermal inkjet technology is widely used for precisely and rapidly dispensing small quantities of fluid. Thermal inkjets eject droplets of fluid out of an orifice by using heating elements to vaporize small portions of the fluid within a firing chamber. The vapor rapidly expands, forcing a small droplet out of the orifice. The heating element is then turned off and the vapor rapidly collapses, drawing more fluid into the firing chamber from a reservoir.
The fluids stored in the reservoir and dispensed through the orifices can absorb and hold gases, such as atmospheric nitrogen, oxygen, or carbon dioxide. Under certain conditions, these gases can come out of the solution and form bubbles. These gas bubbles can become trapped in the firing chambers and prevent drop ejection, resulting in print defects and reduced print quality.
The accompanying drawings illustrate various embodiments of the principles described herein and are a part of the specification. The illustrated embodiments are merely examples and do not limit the scope of the claims.
Throughout the drawings, identical reference numbers designate similar, but not necessarily identical, elements.
As noted above, air bubbles present an issue in inkjet printheads because such bubbles can become trapped in the firing chambers and prevent drop ejection, resulting in print defects or reduced print quality.
Because the bubbles collect gas dissolved in the ink, the bubbles continue to grow and are difficult to remove. However, as will be described herein, creating a flow path into the firing chamber that is more restrictive to bubble growth encourages these bubbles to expand out of the firing nozzle and break, allowing fluid to refill the firing chamber. This has application regardless of the fluid that the device is ejecting. While originally developed to precisely eject ink in printing applications, inkjet technology is now used in a wide variety of fields where a fluid is to be dispensed or ejected with precision. The principles described in this specification may consequently apply to a wide variety of fluids, including ink, being dispensed by an inkjet head.
In the following description, for purposes of explanation, numerous specific details are set forth in order to provide a thorough understanding of the present systems and methods. It will be apparent, however, to one skilled in the art that the present apparatus, systems and methods may be practiced without these specific details. Reference in the specification to “an embodiment,” “an example” or similar language means that a particular feature, structure, or characteristic described in connection with the embodiment or example is included in at least that one embodiment, but not necessarily in other embodiments. The various instances of the phrase “in one embodiment” or similar phrases in various places in the specification are not necessarily all referring to the same embodiment.
Because of the small size of the droplet generator (100), capillary force/surface tension is a predominant force affecting the interaction of fluids with solids or gas. The capillary action occurs when the external intermolecular forces between the liquid and the solid walls are stronger than the cohesive intermolecular forces inside the liquid. The capillary forces tend to draw the fluid into the firing chamber (110) and hold it there.
To eject a droplet from the droplet generator (100), a heating element (200) is proximally located to the firing chamber (110). Electricity is passed through the heating element (200), which causes the temperature of the heating element (200) to rapidly rise and vaporize a small portion of the fluid immediately adjacent to the heating element (200). The vaporization of the fluid creates rapidly expanding vapor which overcomes the capillary forces retaining the fluid within the firing chamber (110) and nozzle (120). As the vapor continues to expand, a droplet is ejected from the nozzle (120).
Following the formation of the vapor bubble, the electrical current through the heating element (200) is cut off and the heating element (200) rapidly cools. The envelope of vaporized fluid collapses, pulling additional fluid from the reservoir into firing chamber (110) to replace the fluid volume vacated by the droplet. Additionally, capillary forces tend to draw the fluid into the firing chamber (110). The droplet generator (100) is then ready to begin a new droplet ejection cycle. Ordinarily, the droplet generators (100) should be full of fluid so that they can consistently eject a droplet toward the printing media.
The flow of fluid through the firing chamber (110) is the primary cooling mechanism for the droplet generator (100). A significant portion of the heat generated by the heating element (200) is absorbed by the surrounding liquid which is then ejected through the nozzle (120).
The size of the droplet that is ejected is determined by the geometry of the firing chamber, the capacity and operation of the heating element, the material properties of the fluid, and other factors. In many cases extremely small drops (with masses of 1-10 nanograms) can be ejected at high frequencies from the firing chamber.
A plurality of droplet generators (100) may be contained within a single fluid-jet or inkjet die. In some circumstances, the inkjet die may be heated using separate resistive heating elements prior to printing. By heating the inkjet die prior to the use of the droplet generators (100); heating surges caused by the individual heating elements (200) within the droplet generators (100) can be minimized. Maintaining an inkjet die in a substantially isothermal state during printing reduces undesirable changes in the printing performance of the die.
As noted above, air bubbles can be a problem within inkjet die because the air bubbles can become trapped in the firing chambers and prevent droplet ejection. One possible mechanism for bubbles to form within the firing chamber is for gas dissolved within the fluid to come out of solution, thereby creating a bubble. The elevated temperature of the inkjet die, in some circumstances, decreases the amount of gas that a fluid can maintain in solution. As the temperature rises, the gas is forced out of the fluid and forms bubbles. The firing chambers, particularly during heavy printing demands, can have higher temperatures than other areas or surfaces that the fluid contacts. Because of the higher temperature, bubbles may be more prone to nucleating within the firing chambers.
As indicated, the elevated temperatures created in thermal inkjet printers encourage air dissolved in the fluid to come out of solution and create bubbles that fill the firing chambers, causing print defects and reduced print quality. When a bubble forms within the firing chamber, the droplet ejection mechanism may no longer be viable. The heating element (200) continues to cycle on and off, but there may be insufficient fluid proximal to the heating element (200) to create a vapor bubble to push fluid out of the firing chamber (110). Additionally, there may be insufficient fluid within the chamber to actually eject a droplet even if a vapor bubble is created. In the absence of fluid flowing through the firing chamber, the temperature of the firing chamber can rise dramatically. The rising temperature within the firing chamber increases the rate at which gas escapes the fluid, thereby causing any bubble nucleating in the firing chamber to increase in size, thereby aggravating the situation. As long as the temperature remains elevated, these bubbles will continue to grow and prevent the firing chamber from functioning.
Air can be removed from the firing chambers by several methods. For example, vacuum priming restores proper function but consumes fluid, thereby increasing costs. Another method is to reduce the head temperature, which decreases the tendency for gasses in the fluid to come out of solution. With faster printing or dispensing speeds, however, lower temperatures cannot always be maintained. Another solution is to use “degassed” fluid in the fluid supplies. The degassing process removes gas dissolved in the fluid to be dispensed, so that such gas cannot later come out of solution and create bubbles. Systems that rely on this method, however, use expensive materials that prevent air from redissolving back into the fluid while the supplies wait for the customer to buy or use the fluid. Even with expensive packaging materials, the fluid can only be protected for a limited amount of time. This limits the effectiveness of the degassing process to relatively high fluid usage customers who will typically consume the fluid after a short period of time.
This internal pressure within the bubble (300) causes the bubble (300) to expand in a direction of least resistance. The direction of least resistance can be defined as the direction in which the bubble (300) can expand with the largest radius of curvature, which typically corresponds to the largest opening or open space at the perimeter of the bubble (300).
In this case, the path of least resistance for the expansion of bubble (300) is through the inlet geometry (155).
The pressure needed to push a bubble (300) through an opening can be defined for a circular orifice by the following equation:
P=(2 σ cos (θ−α))/r (Eq. 1)
As can be seen from the equation above, the pressure needed to push a bubble through a circular opening decreases as the radius of the opening increases. It is easier for a bubble to pass through a large opening than a small opening.
The pressure needed to push a bubble through a rectangular opening, such as the openings created by the throat (150) or islands (130) can be defined by the following equation:
P=(σ cos (θ−α))/(h+w) (Eq. 2)
For the bubbles to be purged from the firing chamber through the nozzle (120), the path of least resistance to expansion needs to be the nozzle (120), not the firing chamber inlet (155). Creating a flow path into the firing chamber (110) that is more restrictive to bubble growth encourages these bubbles to expand out of the nozzle (120) and break, allowing fluid to refill the firing chamber.
By setting Eq. 1 and Eq. 2 equal to each other and assuming that the taper angles a for both the inlet geometry (155) and the nozzle (120) are zero or are small enough to be neglected, the critical nozzle radius can be found for a given inlet geometry.
2/rc=1/h+1/w (Eq. 3)
Solving for the critical radius results in the critical radius being expressed as a function of the height and width of the opposing rectangular opening in the inlet geometry (155).
rc=(2*h*w)/(h+w) (Eq. 4)
When the left side of Eq. 3 or Eq. 4 is equal to the right side of the corresponding Eq. 3 or Eq. 4, the bubble pressure needed to pass through the nozzle and the inlet geometry are equal. The nozzle radius for this condition will be called the critical nozzle radius. Eq. 3 and Eq. 4 describe the situation where resistance to bubble growth is equal in both directions. The two sides of this equation may not necessarily be equal for all printheads. For example, for some self purging printheads it would be expected that the left hand portion of Eq. 3 would be substantially smaller than the right hand side of the same equation. This reflects the lower resistance of the nozzle to the passage of a bubble.
For geometries with a significant taper angle α, it can be shown that:
To obtain a more precise characterization of the critical radius for nozzle geometries with a significant taper angle a, appropriate values can be inserted into Eq. 5.
If the nozzle radius is smaller than the critical nozzle radius, the bubble (300) remains trapped within the firing chamber (110) as shown by
Other parameters within the droplet generator (100) can be altered to reduce the incidence of bubbles within the firing chamber (110). According to one exemplary embodiment, the nozzle (400) is placed as close as possible to the rear wall (420) of the firing chamber (110). By moving the nozzle closer to the back wall, there is a more uniform flow of fluid through the firing chamber. Stagnation points that could occur between the rear wall (420) and the nozzle orifice are minimized, thereby increasing the likelihood that bubbles that form in the stagnation areas will be swept out of the nozzle (400).
Creating self purging fluidic architectures for low drop weight droplet generators can be challenging. For a very small droplet to be generated, the nozzle, inlet geometry, and firing chamber are correspondingly small. In some cases, manufacturing constraints can place a lower limit on dimensions of the inlet or other geometry, resulting in a firing chamber that is not self purging. Recent advances in manufacturing techniques have allowed for smaller inlet structures, enabling self purging architectures even for low drop weight nozzles.
A first double headed arrow (650) represents the diameter of the nozzle (620). In this example, the diameter of the nozzle is 15.2 microns. The radius of the nozzle (620) is half of the diameter, or 7.6 microns. The second double headed arrow (660) represents the limiting rectangular opening within the inlet geometry. In this example, the width of the opening (660) is 5 microns and the vertical height of the opening is 14 microns.
Using Eq. 4 and substituting in the numerical values for the width and height of the inlet opening, it can be found that the critical radius for this design is 7.4 microns. The nozzle radius is 7.6 microns which is greater than the critical radius of 7.4 microns. Because the nozzle radius is greater than the critical radius, it is expected that droplet generator (600) would be self purging. Bubbles that form within the firing chamber (610) would follow the path of least resistance out of nozzle (620) where the bubbles would break, allowing more fluid to pass from the reservoir (640) through the inlet geometry (655) and into the firing chamber (610). The firing chamber (610) would then be ready to resume its normal operation.
In sum, droplet generators can be designed to be self purging as to the formation of gas bubbles from gasses in solution in the printing fluid. This can be accomplished by changing the balance between the inlet and outlet geometries such that the outlet geometry presents a lower resistance to bubble motion and growth Bubbles which then form within the firing chamber naturally exit through the nozzle and break. This allows capillary forces and the droplet generator action to refill the firing chamber. The firing chamber is then ready to operate normally. This self purging geometry allows the firing chambers to be self recovering without adding any cost or complexity to the printing system.
The preceding description has been presented only to illustrate and describe embodiments and examples of the principles described. This description is not intended to be exhaustive or to limit these principles to any precise form disclosed. Many modifications and variations are possible in light of the above teaching.
Filing Document | Filing Date | Country | Kind | 371c Date |
---|---|---|---|---|
PCT/US2007/088421 | 12/20/2007 | WO | 00 | 5/17/2010 |
Publishing Document | Publishing Date | Country | Kind |
---|---|---|---|
WO2009/082391 | 7/2/2009 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
6162589 | Chen et al. | Dec 2000 | A |
7226149 | Stout et al. | Jun 2007 | B2 |
7431434 | Agarwal et al. | Oct 2008 | B2 |
20020060350 | Schulte et al. | May 2002 | A1 |
20040223034 | Feinn et al. | Nov 2004 | A1 |
20050145982 | Chavarria | Jul 2005 | A1 |
20050259123 | Rice et al. | Nov 2005 | A1 |
20050270332 | Strand et al. | Dec 2005 | A1 |
20060028511 | Chwalek et al. | Feb 2006 | A1 |
20060262161 | Rice et al. | Nov 2006 | A1 |
20060268067 | Agarwal et al. | Nov 2006 | A1 |
20070103501 | Hatsui et al. | May 2007 | A1 |
20070194371 | Benjamin | Aug 2007 | A1 |
20070245559 | Feinn et al. | Oct 2007 | A1 |
Number | Date | Country |
---|---|---|
1680278 | Oct 2007 | EP |
Entry |
---|
“Using SU8 primer layer method to control a wicked adhesive in fuse chambers”, Research Disclosure Journal, ISSN 0374-4353. Aug. 2005. pp. 1-3. Research Disclosure Database No. 496053, Kenneth Mason Publications Ltd., The Book Barn, Westbourne, Hants. PO10 8RS. UK. |
Supplementary European Search Report for Application No. EP07869681.2 Report issued Jan. 31, 2011. |
Number | Date | Country | |
---|---|---|---|
20100253748 A1 | Oct 2010 | US |