US3525164A - Apparatus for gaseous treatment of moving webs - Google Patents

Apparatus for gaseous treatment of moving webs Download PDF

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US3525164A
US3525164A US782620A US3525164DA US3525164A US 3525164 A US3525164 A US 3525164A US 782620 A US782620 A US 782620A US 3525164D A US3525164D A US 3525164DA US 3525164 A US3525164 A US 3525164A
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plenum
plate
boxes
headers
walls
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Ernest Charles Brown
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Wolverine Corp
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B21/00Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
    • F26B21/004Nozzle assemblies; Air knives; Air distributors; Blow boxes
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B13/00Machines and apparatus for drying fabrics, fibres, yarns, or other materials in long lengths, with progressive movement
    • F26B13/10Arrangements for feeding, heating or supporting materials; Controlling movement, tension or position of materials

Definitions

  • FIG 5 United States Patent 3,525,164 APPARATUS FOR GASEOUS TREATMENT OF MOVING WEBS Ernest Charles Brown, Danvers, Mass., assignor t0 Wolverine Corporation, Woburn, Mass., a corporation of Massachusetts Filed Dec. 10, 1968, Ser. No. 782,620
  • Apparatus for gaseous treatment of moving webs has a plenum embracing parallel spaced exhaust cross-headers with the spaces between the cross-headers forming outlet passageways from the plenum leading to lower level perforate distributing heads between which are vertical exhaust passageways leading to the exhaust cross-headers so that air impacting on the moving web is drawn away from the moving we b before moving transversely through the cross-headers to discharge points beyond the edges of the moving web.
  • This invention relates to apparatus useful in the gaseous treatment of moving webs, as for drying wet coatings applied to a sheet material.
  • Some coatings for example, those applied to non-porous substrates in the manufacture of photographic film are so thin and fragile that drying the coatings with any substantial forced draft directed towards the coating tends to disperse the coating and fails to produce desired even coating. Yet contact of the material to be dried with a gaseous drying medium having movement relative to the coated surface is desired in order to speed up the drying operation as much as is possible so long as the coating dries uniformly in an even coat, for the greater the quantity of gas contacting the material per unit of time the faster the drying.
  • the difficulty is that, as the velocity of a gaseous drying medium is reduced to prevent disruption of the coating, so much of the potential energy comes to bederived from turbulence alone (it being impossible because of skin and other effects to have truly laminar flow) that the flow is not uniform cross-sectionally.
  • Energy derived from turbulence is dispersed randomly as distinguished from energy derived from static pressure which is dispersed evenly. In some applications then the slight static pressure required for low velocity gas movement contributes so little energy that the total force applied to the medium barely exceeds the force which would anyway be present due to turbulence alone. The result is that the velocity of gas movement varies at different points of impact on the web causing non-uniform drying over the surface area.
  • the present invention provides an air distributing structure which is particularly useful in drying moving webs which can tolerate only very low velocity gaseous impact, e.g., at velocities below 500 linear feet per minute, although the structure can be useful for operations at higher velocities.
  • very low velocity gaseous impact e.g., at velocities below 500 linear feet per minute
  • a resistance distributing head in the form of a perforated plate is placed across each plenum outlet passageway between the exhaust head ers and these passageways then communicate with lower distributing heads in the form of perforated plates which are less open than the upper plates.
  • FIG. 1 is a perspective view of the apparatus with one wall broken away to illustrate internal features
  • FIG. 2 is a transverse cross-sectional view taken through a passageway in the apparatus of FIG. 1, leading downwardly from a plenum;
  • FIG. 3 is a transverse cross-sectional view taken through an exhaust passageway in the apparatus of FIG. 1 leading upwardly to an exhaust header;
  • FIG. 4 is a perspective enlarged view of some portions of the apparatus in an upwardly tilted position.
  • FIG. 5 is a longitudinal cross-sectional fragmentary view showing the construction of the composite bottom Wall of the plenum.
  • the apparatus includes an enclosure 10 through which may be carried, as on appropriate rollers 12 and 14, by virtue of conventional inlet and outlet openings 16 and 18, respectively, a web or film W of coated material to be dried.
  • Each member 20 includes a horizontally extending portion 22 having perpendicularly disposed appendages in the form of a pair of spaced parallel vertical walls 24 spaced inwardly from the side edges of the member 22, one on each side of a row of openings 26 through the portion 22.
  • Both side edges of members 22 have slots 28 formed therein into which may be inserted, between each member 20, a perforated plate 30 connecting the members 20 together.
  • Vertical walls 24 also terminate at the bottom in enlargements in which similar slots 34 are provided into which may be inserted intervening perforated plates 36 connecting the bottoms of the adjoining walls 24 of adjacent members 22 together.
  • one-piece members 20 have on their upper faces vertical slots 38 extending along each side thereof for receiving inverted U-shaped housings 40 forming with the portions 22 crossheaders communicating through openings 26 with exhaust passageways 42 formed between each pair of walls 24.
  • the cross-headers 40 lead to an outlet 44 disposed beyond the side edge of the path of the travelling web to be treated.
  • the enclosure 10 above and surrounding the crossheaders 40 thus forms a plenum 50 having top inlets 51 and communicating with the spaces 52 forming vertical passageways between cross-headers 40.
  • a fan or other conventional air mover 54 is placed in the cross-header outlets 44 to create a differential pressure between air in plenum 50 and in the cross-headers 40 thereby creating air flow from plenum 50 down through vertical passageways 52, through apertured plate 30, through apertured plate 36 against the web W, the air then travelling longitudinally of the web symmetrically to and up the exhaust passageways 42 between walls 24, through openings 26 and into the cross-headers 40.
  • the configuration of the bottom wall of the plenum can thus be described as being a series of hollow boxes connected together in staggered relation in upper and lower rows, the upper row boxes being defined by walls 40 and 22 and the lower row boxes by walls 24 and intervening upper and lower plates 30 and 36.
  • the bottom walls 22 of the upper row boxes have openings 26 and both top and bottom walls 30 and 36 of the lower row boxes have openings therein, being perforated.
  • plate 36 may have, for example, 22.5% open area and plate 30, 90% open area in a construction wherein the passageways 52 are 3 inches wide and the exhaust passageways 42, 1 inch wide. This gives a five to one ratio of total open area between the upper plate 30 and the lower plate 36. Accordingly, in operation, if the pressure in the plenum is of the order of .25 to .76 inch water column, the static pressure between the plates will be of the order of .01 and .03 inch water column.
  • the exhaust gas at openings 26 may then have a velocity of 2300 to 4000 feet per minute with an intake at plate 30 of about 2000 to 3500 feet per minute. This provides a flow from plate 36 in the order of between 72 and 126 cubic feet per minute where the passageways 52 and 42 are five feet long transversely of the apparatus.
  • the plate 30 may be dispensed with entirely and of course it will be under stood that by virtue of the slot construction for insertion of the plates 30 and 36, they may be readily replaced with plates having varying open areas and/or size of perforations depending upon the type of operation desired.
  • the apertures 26 are inch in diameter
  • the slots in the members 20 are not essential to the invention since the plates may be otherwise supported, nor is it essential that the members 20 be of one piece construction, though when they are and are fabricated by extrusion, assembly is conveniently simple.
  • Apparatus for gaseous treatment of moving webs comprising walls forming a plenum
  • one of the walls of said plenum being a horizontally extending composite wall which includes:
  • headers forming therebetween inner extensions of the intervening vertical passageways in said outer row, and forming therewith outlet passageways from said plenum
  • Apparatus for gaseous treatment of moving webs comprising walls forming a plenum
  • one of the walls of said plenum being a horizontally extending composite wall which includes a series of hollow boxes connected together in staggered relation in upper and lower rows, the boxes in each row being spaced from one another longitudinally of said plenum,
  • each of said one-piece members comprising:
  • said legs including portions defining oppositely outwardly facing slots extending along the marginal bottom edge portions of said legs slidably receiving 8,525,164 5 6 and supporting one edge of adjacent perforated and outwardly of a plenum of which said composite plates, and wall forms one wall.

Description

5, 1970 E. c. BROWN 3,525,164
APPARATUS FOR GASEOUS TREATMENT MOVING WEBS 2 SheetS-Sheet 1 FIG Filed Dec. 10, 1968 I IZ FIG 2 E. C. BROWN Aug. 25, 1970 I APPARATUS FOR GASEOUS TREATMENT OF MOVING WE BS 2 Sheets-Sheet 2 Filed Dec. 10, 1968 ,A MW) FIG 5 United States Patent 3,525,164 APPARATUS FOR GASEOUS TREATMENT OF MOVING WEBS Ernest Charles Brown, Danvers, Mass., assignor t0 Wolverine Corporation, Woburn, Mass., a corporation of Massachusetts Filed Dec. 10, 1968, Ser. No. 782,620
Int. Cl. F26b 23/00 US. Cl. 34-155 Claims ABSTRACT OF THE DISCLOSURE Apparatus for gaseous treatment of moving webshas a plenum embracing parallel spaced exhaust cross-headers with the spaces between the cross-headers forming outlet passageways from the plenum leading to lower level perforate distributing heads between which are vertical exhaust passageways leading to the exhaust cross-headers so that air impacting on the moving web is drawn away from the moving we b before moving transversely through the cross-headers to discharge points beyond the edges of the moving web.
This invention relates to apparatus useful in the gaseous treatment of moving webs, as for drying wet coatings applied to a sheet material.
Some coatings, for example, those applied to non-porous substrates in the manufacture of photographic film are so thin and fragile that drying the coatings with any substantial forced draft directed towards the coating tends to disperse the coating and fails to produce desired even coating. Yet contact of the material to be dried with a gaseous drying medium having movement relative to the coated surface is desired in order to speed up the drying operation as much as is possible so long as the coating dries uniformly in an even coat, for the greater the quantity of gas contacting the material per unit of time the faster the drying.
The difficulty is that, as the velocity of a gaseous drying medium is reduced to prevent disruption of the coating, so much of the potential energy comes to bederived from turbulence alone (it being impossible because of skin and other effects to have truly laminar flow) that the flow is not uniform cross-sectionally. Energy derived from turbulence is dispersed randomly as distinguished from energy derived from static pressure which is dispersed evenly. In some applications then the slight static pressure required for low velocity gas movement contributes so little energy that the total force applied to the medium barely exceeds the force which would anyway be present due to turbulence alone. The result is that the velocity of gas movement varies at different points of impact on the web causing non-uniform drying over the surface area.
In a structure such as is shown and described in my Pat. No. 3,398,466, for example, if the velocities at the slots 39 are reduced below 500 feet per minute, most of the potential energy is derived from turbulence, and there is such little control of the exhausting gases in the spaces around the plenum 12 that a web being treated receives impacts at randomly varying velocities and uniform drying across the web is not achieved.
The present invention provides an air distributing structure which is particularly useful in drying moving webs which can tolerate only very low velocity gaseous impact, e.g., at velocities below 500 linear feet per minute, although the structure can be useful for operations at higher velocities. By using cross-headers within a plenum for exhausting the gases rather than cross-headers outside the plenum for the ingoing gas, I have found that so much better control of the exhaust gases is secured as to elimiice nate random variation in velocity of low velocity gas at impact, at least so far as can be determined from finished dried products. Accordingly, I expose a distributing head to the static pressure of a gas in a plenum which embraces a series of spaced exhaust cross-headers. Additionally, in accordance with this invention, a resistance distributing head in the form of a perforated plate is placed across each plenum outlet passageway between the exhaust head ers and these passageways then communicate with lower distributing heads in the form of perforated plates which are less open than the upper plates.
In this manner the pressure in the plenum maybe considerable while the pressure between the plates is less and such as to produce a very gentle low velocity draft of extremely evenly distributed impact with much increased velocity at the ingress to the exhaust headers.
The structure is also much simplified because tubes, such as are used in US. Pat. No. 3,398,466 are no longer required,
Apparatus in accordance with the present invention is shown in the drawings wherein:
FIG. 1 is a perspective view of the apparatus with one wall broken away to illustrate internal features;
FIG. 2 is a transverse cross-sectional view taken through a passageway in the apparatus of FIG. 1, leading downwardly from a plenum;
'FIG. 3 is a transverse cross-sectional view taken through an exhaust passageway in the apparatus of FIG. 1 leading upwardly to an exhaust header;
FIG. 4 is a perspective enlarged view of some portions of the apparatus in an upwardly tilted position; and
FIG. 5 is a longitudinal cross-sectional fragmentary view showing the construction of the composite bottom Wall of the plenum.
The apparatus includes an enclosure 10 through which may be carried, as on appropriate rollers 12 and 14, by virtue of conventional inlet and outlet openings 16 and 18, respectively, a web or film W of coated material to be dried.
Superposed over the web is an air distributing system which, for convenience, will be described from the bottom up and as best can be seen in FIG. 4. A series of transverse one-piece members 20 are supported in spaced relation across the enclosure above the path of the web W. Each member 20 includes a horizontally extending portion 22 having perpendicularly disposed appendages in the form of a pair of spaced parallel vertical walls 24 spaced inwardly from the side edges of the member 22, one on each side of a row of openings 26 through the portion 22.
Both side edges of members 22 have slots 28 formed therein into which may be inserted, between each member 20, a perforated plate 30 connecting the members 20 together.
, Vertical walls 24 also terminate at the bottom in enlargements in which similar slots 34 are provided into which may be inserted intervening perforated plates 36 connecting the bottoms of the adjoining walls 24 of adjacent members 22 together.
Lastly, one-piece members 20 have on their upper faces vertical slots 38 extending along each side thereof for receiving inverted U-shaped housings 40 forming with the portions 22 crossheaders communicating through openings 26 with exhaust passageways 42 formed between each pair of walls 24.
As shown in FIG. 3, the cross-headers 40 lead to an outlet 44 disposed beyond the side edge of the path of the travelling web to be treated.
The enclosure 10 above and surrounding the crossheaders 40 thus forms a plenum 50 having top inlets 51 and communicating with the spaces 52 forming vertical passageways between cross-headers 40.
A fan or other conventional air mover 54 is placed in the cross-header outlets 44 to create a differential pressure between air in plenum 50 and in the cross-headers 40 thereby creating air flow from plenum 50 down through vertical passageways 52, through apertured plate 30, through apertured plate 36 against the web W, the air then travelling longitudinally of the web symmetrically to and up the exhaust passageways 42 between walls 24, through openings 26 and into the cross-headers 40.
The configuration of the bottom wall of the plenum can thus be described as being a series of hollow boxes connected together in staggered relation in upper and lower rows, the upper row boxes being defined by walls 40 and 22 and the lower row boxes by walls 24 and intervening upper and lower plates 30 and 36. The bottom walls 22 of the upper row boxes have openings 26 and both top and bottom walls 30 and 36 of the lower row boxes have openings therein, being perforated.
The perforations in plate 30 are larger than those in plate 36 but plate 36 may have, for example, 22.5% open area and plate 30, 90% open area in a construction wherein the passageways 52 are 3 inches wide and the exhaust passageways 42, 1 inch wide. This gives a five to one ratio of total open area between the upper plate 30 and the lower plate 36. Accordingly, in operation, if the pressure in the plenum is of the order of .25 to .76 inch water column, the static pressure between the plates will be of the order of .01 and .03 inch water column. The exhaust gas at openings 26 may then have a velocity of 2300 to 4000 feet per minute with an intake at plate 30 of about 2000 to 3500 feet per minute. This provides a flow from plate 36 in the order of between 72 and 126 cubic feet per minute where the passageways 52 and 42 are five feet long transversely of the apparatus.
It is to be understood that in some cases where extremely low velocities are not required, the plate 30 may be dispensed with entirely and of course it will be under stood that by virtue of the slot construction for insertion of the plates 30 and 36, they may be readily replaced with plates having varying open areas and/or size of perforations depending upon the type of operation desired. In the form shown, the apertures 26 are inch in diameter, the apertures in plate 30, inch in diameter and the apertures in plate 36, V inch in diameter. Also, the slots in the members 20 are not essential to the invention since the plates may be otherwise supported, nor is it essential that the members 20 be of one piece construction, though when they are and are fabricated by extrusion, assembly is conveniently simple.
What is claimed is:
1. Apparatus for gaseous treatment of moving webs comprising walls forming a plenum,
one of the walls of said plenum being a horizontally extending composite wall which includes:
spaced transverse vertical walls forming therebetween an outer aligned row of parallel vertical passageways,
a series of spaced hollow cross-headers, each spanning the inner end of an alternate passageway of said row and having intake openings communicating therewith and having an end outlet for discharging air outside of said plenum,
said headers forming therebetween inner extensions of the intervening vertical passageways in said outer row, and forming therewith outlet passageways from said plenum,
a series of perforate plates, each spanning one of said outlet passageways for distributing gas passing therethrough, and
means for maintaining a differential lower pressure in said headers than in said plenum to draw gaseous fluid continuously from said plenum through said outlet passageways against a web passing beneath said composite wall, around free edges of said vertical walls into the alternating outer vertical passageways and thence through said intake openings into the cross-headers and thence to said cross-header outlets for discharge outside said plenum beyond the path of said moving web.
2. Apparatus as claimed in claim. 1, wherein said crossheaders are wider than said alternate outer row passagewaysand said plenum outlet passageways have narrow inner portions between said headers and wider outer portions between said vertical walls.
3. Apparatus as claimed in claim 1, wherein said perforate plates lie in a single plane intersecting the outer ends of said plenum outlet passageways.
4. Apparatus as claimed in claim 1, wherein said series of perforate plates include an outer and an inner plate spanning each plenum outlet passageway.
5. Apparatus as claimed in claim 4, wherein the perforations in said inner plates are larger than the perforations in said outer plates.
6. Apparatus as claimed in claim 2, wherein said series of perforate plates include outer plates lying in one plane across said wider Outer portions of said plenum outlet passageways and inner plates lying in a different plane across said narrow portions of said plenum outlet passageways.
7. Apparatus for gaseous treatment of moving webs comprising walls forming a plenum,
one of the walls of said plenum being a horizontally extending composite wall which includes a series of hollow boxes connected together in staggered relation in upper and lower rows, the boxes in each row being spaced from one another longitudinally of said plenum,
the bottom walls of the boxes in said upper row having openings therein communicating with the spaces between the boxes in the lower row,
the top walls of the boxes in the lower row having openings therein communicating with the spaces between the boxes in the upper row,
the bottom walls of the boxes in the lower row being perforated,
and means for maintaining a differential lower pressure in said upper row of boxes than in said plenum to draw gaseous fluid continuously from said plenum through said lower row bottom wall perforations against a web passing beneath said composite wall and then away from said web through said openings in the bottom walls of the upper row boxes into said upper row boxes and then laterally through said upper row boxes for discharge beyond the path of said moving web.
8. Apparatus as claimed in claim 7, wherein said boxes in the upper and lower rows symmetrically partially overlap one another.
9. Apparatus as claimed in claim 7 wherein the openings in the top walls of the boxes in the lower row are perforations in the portions of said top walls lying between said boxes in the upper row.
10. As a composite plenum wall, a series of one-piece strgctural members arranged in parallel spaced relation, an
perforated plates extending between said members,
each of said one-piece members comprising:
an elongated plate having a series of medially aligned openings,
a pair of parallel spaced legs extending from one side of said plate normal to said plate, one on each side of said series of openings, but spaced inwardly from the longitudinal side edges of said plate,
said legs including portions defining oppositely outwardly facing slots extending along the marginal bottom edge portions of said legs slidably receiving 8,525,164 5 6 and supporting one edge of adjacent perforated and outwardly of a plenum of which said composite plates, and wall forms one wall. marginal edge portions of said plate defining a pair of References Cited parallel slots on the opposite side of said plate from said legs and facing away from said plate for re- 5 UNITED STATES PATENTS ceiving the bottom edges of an inverted U-shaped 3,371,427 3/ 1968 yg 34155 housing to form cross-headers for conveying gas 3,453,743 7/ 1969 Hale 34155 passing p y through said openings transversely EDWARD J. MICHAEL, Primary Examiner
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Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3771235A (en) * 1970-12-29 1973-11-13 Fuji Photo Film Co Ltd Method for floating and drying a web
US3771239A (en) * 1970-12-30 1973-11-13 Fuji Photo Film Co Ltd Apparatus for drying a web by use of an air jet flow
JPS5065961A (en) * 1973-10-10 1975-06-03
US3895449A (en) * 1973-10-10 1975-07-22 Beloit Corp Air impingement system
US3936953A (en) * 1973-10-10 1976-02-10 Beloit Corporation Air impingement system
WO1982003450A1 (en) * 1981-03-27 1982-10-14 Kodak Co Eastman Method and apparatus for drying coated sheet material
US4776107A (en) * 1987-10-30 1988-10-11 Wolverine Corporation Web treatment system
US4868999A (en) * 1987-03-20 1989-09-26 C.D. High Technology Apparatus and method for production of asphalt pavement having high recycled asphalt content
EP0465950A1 (en) * 1990-07-07 1992-01-15 BASF Aktiengesellschaft Contact belt dryer
EP0652412A1 (en) * 1993-11-05 1995-05-10 Schmitz + Apelt LOI Industrieofenanlagen GmbH Industrial furnace for the thermic treatment of a load in a treatment chamber
US20060123656A1 (en) * 2002-05-08 2006-06-15 Secomak Ltd. Method and apparatus for de-watering articles
US20070227034A1 (en) * 2006-03-30 2007-10-04 Fujifilm Corporation Method and apparatus for drying coated film, and method for manufacturing optical film
EP1921407A2 (en) * 2006-11-09 2008-05-14 Deutsche Mechatronics GmbH Drying system
ITPC20110001A1 (en) * 2011-01-11 2012-07-12 Nordmeccanica Spa PLANT FOR DRYING A COVERED FILM CONTINUOUSLY
US20130125414A1 (en) * 2011-11-21 2013-05-23 Hon Hai Precision Industry Co., Ltd. Blow drying mechanism for workpieces
FR3030705A1 (en) * 2014-12-17 2016-06-24 Andritz Perfojet Sas INSTALLATION FOR DRYING A WET NON-WOVEN NET

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3371427A (en) * 1965-09-14 1968-03-05 Proctor & Schwartz Inc Apparatus for processing web material
US3453743A (en) * 1967-06-08 1969-07-08 Thomas F Hale Veneer dryer

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3371427A (en) * 1965-09-14 1968-03-05 Proctor & Schwartz Inc Apparatus for processing web material
US3453743A (en) * 1967-06-08 1969-07-08 Thomas F Hale Veneer dryer

Cited By (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3771235A (en) * 1970-12-29 1973-11-13 Fuji Photo Film Co Ltd Method for floating and drying a web
US3771239A (en) * 1970-12-30 1973-11-13 Fuji Photo Film Co Ltd Apparatus for drying a web by use of an air jet flow
JPS5065961A (en) * 1973-10-10 1975-06-03
US3895449A (en) * 1973-10-10 1975-07-22 Beloit Corp Air impingement system
US3936953A (en) * 1973-10-10 1976-02-10 Beloit Corporation Air impingement system
JPS5818589B2 (en) * 1973-10-10 1983-04-13 ベロイト コ−ポレ−ション Koushiyougekishiki Kansou Souchi
WO1982003450A1 (en) * 1981-03-27 1982-10-14 Kodak Co Eastman Method and apparatus for drying coated sheet material
US4365423A (en) * 1981-03-27 1982-12-28 Eastman Kodak Company Method and apparatus for drying coated sheet material
US4868999A (en) * 1987-03-20 1989-09-26 C.D. High Technology Apparatus and method for production of asphalt pavement having high recycled asphalt content
US4776107A (en) * 1987-10-30 1988-10-11 Wolverine Corporation Web treatment system
EP0465950A1 (en) * 1990-07-07 1992-01-15 BASF Aktiengesellschaft Contact belt dryer
EP0652412A1 (en) * 1993-11-05 1995-05-10 Schmitz + Apelt LOI Industrieofenanlagen GmbH Industrial furnace for the thermic treatment of a load in a treatment chamber
US20060123656A1 (en) * 2002-05-08 2006-06-15 Secomak Ltd. Method and apparatus for de-watering articles
US20070227034A1 (en) * 2006-03-30 2007-10-04 Fujifilm Corporation Method and apparatus for drying coated film, and method for manufacturing optical film
EP1921407A2 (en) * 2006-11-09 2008-05-14 Deutsche Mechatronics GmbH Drying system
EP1921407A3 (en) * 2006-11-09 2009-12-16 Deutsche Mechatronics GmbH Drying system
AU2012206324B2 (en) * 2011-01-11 2015-03-05 Nordmeccanica Spa Plant for continuously drying a coated film
WO2012095791A1 (en) * 2011-01-11 2012-07-19 Nordmeccanica Spa Plant for continuously drying a coated film
ITPC20110001A1 (en) * 2011-01-11 2012-07-12 Nordmeccanica Spa PLANT FOR DRYING A COVERED FILM CONTINUOUSLY
US10168097B2 (en) 2011-01-11 2019-01-01 Nordmeccanica S.P.A. Plant for continuously drying a coated film
US20130125414A1 (en) * 2011-11-21 2013-05-23 Hon Hai Precision Industry Co., Ltd. Blow drying mechanism for workpieces
FR3030705A1 (en) * 2014-12-17 2016-06-24 Andritz Perfojet Sas INSTALLATION FOR DRYING A WET NON-WOVEN NET
EP3034976A3 (en) * 2014-12-17 2016-08-17 ANDRITZ Perfojet SAS Installation for drying a wet non-woven web
EP3141853A1 (en) * 2014-12-17 2017-03-15 ANDRITZ Perfojet SAS Installation for drying a wet non-woven web
US20170227286A1 (en) * 2014-12-17 2017-08-10 Andritz Perfojet Sas Installation for drying a damp non-woven web
US9765480B2 (en) 2014-12-17 2017-09-19 Andritz Perfojet Sas Installation for drying a damp non-woven web
US10113268B2 (en) * 2014-12-17 2018-10-30 Andritz Perfojet Sas Installation for drying a damp non-woven web

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