In some high speed inkjet web printers, often called web presses, the first side of the web is printed at a first printing unit, the web is inverted, and then the second side of the web is printed at a second printing unit. The web is guided through a dryer after each side is printed to dry the ink.
The same part numbers designate the same or similar parts throughout the figures.
Inkjet web presses can benefit from the use of higher water content inks. Higher water content inks, however, increase the need for higher capacity dryers, particular to support fast printing speeds. Of course, it is desirable to minimize the size and cost of the press and the cost of operating the press. A new dryer has been developed to help increase drying capacity in high speed inkjet web presses while minimizing any increase in size and cost associated with the added drying capacity. In one example, each successive stage of a multi-stage dryer is configured to take in air discharged from a prior stage, reheat the air and discharge it on to the web moving through the dryer from the last dryer stage to the first dryer stage, such that the web is exposed to the highest humidity air first in the dryer and to the lowest humidity air last in the dryer. As described in detail below, humidity generated in the drying process is used beneficially to promote dryer efficiency. Also, unlike conventional hot air dryers that use one blower to handle air flow, multiple smaller blowers may be used for better flow control to further improve drying efficiency.
Examples of the new dryer and drying process are not limited to inkjet web presses or to printing in general, but may be implemented in other devices and for other applications. Accordingly, the examples described herein and shown in the Figures illustrate but do not limit the invention.
Each successive dryer stage 16, 18 and 20 is configured to take in air discharged from a prior stage 14, 16 and 18, respectively, reheat the air and discharge it on to article 22 moving through dryer 10 from the last stage 20 to the first stage 14 such that article 22 is exposed to the highest humidity air first in dryer 10 and to the lowest humidity air last in dryer 10. In operation, at first dryer stage 14, ambient air is heated and pumped into discharge chamber 42 and on to article 22 where it picks up moisture from article 22, which is at the last part of its passage through dryer 10. The now more humid air discharged on to article 22 at first dryer stage 14 is collected in return chamber 50. At second dryer stage 16, air from return chamber 50 is heated and pumped into discharge chamber 44 and on to article 22 where it picks up more moisture from article 22, which is at a middle part of its passage through dryer 10.
The now more humid air discharged on to article 22 at second dryer stage 16 is collected in return chamber 52. At third dryer stage 18, air from return chamber 52 is heated and pumped into discharge chamber 46 and on to article 22 where it picks up more moisture from article 22, which is at a middle part of its passage through dryer 10. The now more humid air discharged on to article 22 at third dryer stage 18 is collected in return chamber 54. At the fourth and last dryer stage 20, air from return chamber 54 is heated and pumped into discharge chamber 48 and on to article 22, which is at the first part of its passage through dryer 10. If desired, the air discharged on to article 22 at fourth dryer stage 20 may be collected in a chamber 56 and actively exhausted through a blower 58.
While each return chamber 50, 52, 54 is associated with a prior dryer stage 14, 16, 18, respectively, in the above description, each such return chamber 50, 52, 54 could be associated with the corresponding successive dryer stage 16, 18, 20. Whichever association is used, each return chamber is used to supply air from a prior dryer stage to a successive dryer stage.
Referring now specifically to
Airflow is managed in dryer 10 by breaking up the convective air zone into multiple stages in which each successive stage utilizes moisture removed from article 22 in the prior stage. Hot humid air is efficient at heat transfer—getting heat energy to the article to be dried. Hot dry air is efficient at mass transfer—evaporating moisture from the article. The higher humidity of the hot air applied to article 22 first in dryer 10 at the later dryer stage(s) promotes heat transfer, heating article 22 to the desired temperature faster than if drier air were applied. The progressively dryer hot air applied to article 22 at the earlier dryer stages promotes mass transfer, accelerating evaporation to the desired dryness. This type of multi-stage dryer can also realize energy efficiency by reusing heat still in the air discharged from each prior stage. Configurations for a dryer 10 other than the examples shown in the figures are possible. For example, it may be desirable in some implementations to use more or fewer dryer stages, other paths for the article to be dried, and/or with other arrangements for the discharge and return chambers.
As used in the Claims, “a” and “an” mean one or more.
As noted at the beginning of this Description, the examples shown in the figures and described above illustrate but do not limit the invention. Other examples may be made and implemented. Therefore, the foregoing description should not be construed to limit the scope of the invention, which is defined in the following claims.
Filing Document | Filing Date | Country | Kind |
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PCT/US2013/057240 | 8/29/2013 | WO | 00 |
Publishing Document | Publishing Date | Country | Kind |
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WO2015/030766 | 3/5/2015 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
3377056 | Boye | Apr 1968 | A |
5383288 | Ilmarinen | Jan 1995 | A |
5657555 | Milojevic et al. | Aug 1997 | A |
5713138 | Rudd | Feb 1998 | A |
6311410 | Heikkila et al. | Nov 2001 | B1 |
6473997 | Berg | Nov 2002 | B1 |
6877247 | DeMoore | Apr 2005 | B1 |
8046934 | Lenoir | Nov 2011 | B2 |
20120260518 | Melgaard et al. | Oct 2012 | A1 |
20130215202 | Koller et al. | Aug 2013 | A1 |
20150174924 | Fuchioka et al. | Jun 2015 | A1 |
Number | Date | Country |
---|---|---|
0704043 | Jun 1998 | EP |
2553085 | Apr 1985 | FR |
2007192528 | Aug 2007 | JP |
2011121193 | Jun 2011 | JP |
2012051156 | Mar 2012 | JP |
2013107211 | Jun 2013 | JP |
WO-8908809 | Sep 1989 | WO |
WO-2012175810 | Dec 2012 | WO |
Entry |
---|
Deventer, H.C.V.; Feasibility of Energy Efficient Steam Drying of Paper and Textile Including Process Integration. |
International Searching Authorty. International Search Report. Date of mailing May 19, 2014. Application No. PCT/US2013/057240. Mail date Aug. 29, 2013. |
Number | Date | Country | |
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20160214405 A1 | Jul 2016 | US |