US3638604A - Apparatus for coating strip-form substrates - Google Patents

Apparatus for coating strip-form substrates Download PDF

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Publication number
US3638604A
US3638604A US797809A US3638604DA US3638604A US 3638604 A US3638604 A US 3638604A US 797809 A US797809 A US 797809A US 3638604D A US3638604D A US 3638604DA US 3638604 A US3638604 A US 3638604A
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United States
Prior art keywords
chamber
pressure
narrow gap
coating
gap
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Expired - Lifetime
Application number
US797809A
Inventor
Peter Herzhoff
Hans Gref
Rolf Behr
Fritz Maus
Wolfgang Schweicher
Willi Wasser
Josef Friedsam
Kurt Browatzki
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Agfa Gevaert AG
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Agfa Gevaert AG
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05DPROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05D1/00Processes for applying liquids or other fluent materials
    • B05D1/26Processes for applying liquids or other fluent materials performed by applying the liquid or other fluent material from an outlet device in contact with, or almost in contact with, the surface
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/07Flat, e.g. panels
    • B29C48/08Flat, e.g. panels flexible, e.g. films
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/30Extrusion nozzles or dies
    • B29C48/305Extrusion nozzles or dies having a wide opening, e.g. for forming sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/30Extrusion nozzles or dies
    • B29C48/35Extrusion nozzles or dies with rollers
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H23/00Processes or apparatus for adding material to the pulp or to the paper
    • D21H23/02Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
    • D21H23/22Addition to the formed paper
    • D21H23/46Pouring or allowing the fluid to flow in a continuous stream on to the surface, the entire stream being carried away by the paper
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H5/00Special paper or cardboard not otherwise provided for
    • D21H5/0005Processes or apparatus specially adapted for applying liquids or other fluent materials to finished paper or board, e.g. impregnating, coating
    • D21H5/0042Processes or apparatus specially adapted for applying liquids or other fluent materials to finished paper or board, e.g. impregnating, coating by pouring or allowing to flow in a continuous stream onto the surface, the entire stream being carried away by the paper
    • GPHYSICS
    • G03PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
    • G03CPHOTOSENSITIVE MATERIALS FOR PHOTOGRAPHIC PURPOSES; PHOTOGRAPHIC PROCESSES, e.g. CINE, X-RAY, COLOUR, STEREO-PHOTOGRAPHIC PROCESSES; AUXILIARY PROCESSES IN PHOTOGRAPHY
    • G03C1/00Photosensitive materials
    • G03C1/74Applying photosensitive compositions to the base; Drying processes therefor

Definitions

  • the feed means contains a chamber opening into the narrow gap, and the machine is arranged so Filedl 1 that the viscous emulsion fed from the chamber and formed by the narrow gap is under an adjustable static differential in [211 Appl- 797809 pressure between the inlet end of the narrow gap which has a lower pressure on the emulsion and the outlet end of the gap [52] U.S. Cl ..118/50, 1 18/410 which has a higher pressure.
  • .rBOSc 5/02 chamber in the feed means has one opening into the chamber [58] Field of Search .1 18/50, 410, 41 1,412, 50.1 sidewall and containing a compressible gas acts as an air cushion and reduces the variations in pressure on the feed [56] References Cited material during feeding as the gas is enclosable within the cavity by the passage of feed material through the chamber. UNITED STATES PATENTS 3,067,060 12/1962 Glaus ..1' 18/324 x 2 Clams 1 Draw PATENTEDFEB HHTZ 3.538.604
  • This invention relates to a process for coating substrates in strip form with viscous solutions, preferably with photographic emulsions, in which the substrate is wetted in a sealed coating chamber whose end at the point where the emulsion emerges is formed by a coating gap several times wider than the wet finished layer is thick, and in which to counteract the forward movement of the moved substrate, layer formation is effected under an adjustable static pressure differential between the inlet end and outlet end of the gap, the lower pressure prevailing at the inlet end.
  • this alternating pressure emanating from vibration can be reduced to a harmless extent by providing inside the emulsion chamber of the coating machine a cavity in which a cushion of air is enclosed when the coating chamber is full.
  • This cavity advantageously extends over the entire width or almost over the entire width of the coating machine.
  • both the air and the emulsion volume behave like two series-arranged elastic media the softer of which, namely the air, eventually determines the amplitude of the alternating pressure created.
  • the amplitude of this alternating pressure is proportional to the resistance of the medium of sound waves.
  • the resistance of air to sound wave is lower by a factor of 3,600
  • the residual-alternating pressure amplitude is three to four times smaller than the static pressure differential governing layer thickness at the coating gap, with the result that it is no longer able to produce any noticeable cross cut in the coating.
  • a roll 5 provides a rotatable support for the substrate to be coated as it passes the coating machine 4.
  • a gap 6 is defined between the substrate supported by the roll 5 and the coating machine 4.
  • a chamber 3 at the inlet end of the machine provides a low pressure at the inlet end of the gap.
  • the coating machine 4 is provided with an internal emulsion chamber 2 which is supplied with coating material as indicated by the arrow in the drawing.
  • a cavity 1, in which a cushion of air is provided, is in communication with the chamber 2.
  • an apparatus for coating a layer of viscous material on a movable substrate which includes the combination of a movable substrate, a sealed coating chamber for wetting the substrate, a viscous material for feeding onto said movable substrate, a coating machine for depositing the viscous material on the substrate containing the sealed coating chamber and being operatively associated with the substrate having one end associated with the substrate so as to form a narrow gap between the coating machine and the substrate, the gap having an inlet end at which the substrate enters the gap and an outlet end at which the substrate departs from the gap, and including means in the combination or applying a static pressure differential at a lower pressure at the inlet end and a higher pressure at the outlet end of the narrow gap, and in which the viscous material is fed from the coating machine through an opening from the chamber into the narrow gap, the improvement consisting of a cavity laterally adjoining the said chamber having an opening into the chamber through a chamber sidewall and containing a compressible gas, said gas being encloseable within said cavity by said conveyed vis

Abstract

A machine for coating a layer of a viscous emulsion on a movable support having a feed means operatively associated with the support with a narrow gap between the feed means and the support for forming the viscous emulsion into a layer on the movable support. The feed means contains a chamber opening into the narrow gap, and the machine is arranged so that the viscous emulsion fed from the chamber and formed by the narrow gap is under an adjustable static differential in pressure between the inlet end of the narrow gap which has a lower pressure on the emulsion and the outlet end of the gap which has a higher pressure. A cavity in a wall-adjoining the chamber in the feed means has one opening into the chamber sidewall and containing a compressible gas acts as an air cushion and reduces the variations in pressure on the feed material during feeding as the gas is enclosable within the cavity by the passage of feed material through the chamber.

Description

United States atent Herzhoif et al. 1 1 Feb. 1, 1972 [54] APPARATUS FOR COATING STRIP- 3,206,323 9/1965 Miller et al ..118/50 X FORM SUBSTRATES Primary Examiner-John P. McIntosh [72] Inventors: Peter Herzhoff, Leverkusen; Hans Gref, c n and Hutz Cologne-Stammherm; Rolf Behr, Leverkusen; Fritz Maus, CologneFlittard; [57] ABSTRACT Wolfgang Schweicher; Willi Wasser, both of Level-kusen; Josef Friedsam, A machine for coating a layer of a viscous emulsion on a Langenfeld; Kurt Bmwatzki, opladenq movable support having a feed means operatively associated all Germany with the support with a narrow gap between the feed means [73 1 Assignce. Agfa cevaert Akfiengeseuschafl Lave and the support for forming the viscous emulsion into a layer kusen, Germany on the movable support. The feed means contains a chamber opening into the narrow gap, and the machine is arranged so Filedl 1 that the viscous emulsion fed from the chamber and formed by the narrow gap is under an adjustable static differential in [211 Appl- 797809 pressure between the inlet end of the narrow gap which has a lower pressure on the emulsion and the outlet end of the gap [52] U.S. Cl ..118/50, 1 18/410 which has a higher pressure. A cavity in a wall-adjoining the [51] Int. Cl. .rBOSc 5/02 chamber in the feed means has one opening into the chamber [58] Field of Search .1 18/50, 410, 41 1,412, 50.1 sidewall and containing a compressible gas acts as an air cushion and reduces the variations in pressure on the feed [56] References Cited material during feeding as the gas is enclosable within the cavity by the passage of feed material through the chamber. UNITED STATES PATENTS 3,067,060 12/1962 Glaus ..1' 18/324 x 2 Clams 1 Draw PATENTEDFEB HHTZ 3.538.604
INVENTOR I;:
APPARATUS FOR COATING STRIP-FORM SUBSTRATES This invention relates to a process for coating substrates in strip form with viscous solutions, preferably with photographic emulsions, in which the substrate is wetted in a sealed coating chamber whose end at the point where the emulsion emerges is formed by a coating gap several times wider than the wet finished layer is thick, and in which to counteract the forward movement of the moved substrate, layer formation is effected under an adjustable static pressure differential between the inlet end and outlet end of the gap, the lower pressure prevailing at the inlet end.
It has been found in practice that static pressure differentials equivalent to a water column of from 20 to 250 mm. are needed to form the required thicknesses with conventional emulsions.
One disadvantage affecting the practical application of the process is that an alternating pressure is superimposed upon the static pressure difierential as a result of inevitable vibration in the coater, producing periodically alternating thick and thin zones, so-called cross cuts," in the emulsion layer leaving the coater. For example, vibrations affecting the coater at a frequency of 25 c./s. are inevitable despite careful antivibration screening on account of the three-phase motors which rotate in the coating machine at a speed of approximately 1,500 r.p.m., corresponding to 25 c./s. If this vibration has an amplitude of only 2;; for example, this gives rise to an alternating pressure of approximately 50 mm. of water, in other words a value which is comparable to the static pressure differential governing layer thickness.
It has now been found that this alternating pressure emanating from vibration can be reduced to a harmless extent by providing inside the emulsion chamber of the coating machine a cavity in which a cushion of air is enclosed when the coating chamber is full. This cavity advantageously extends over the entire width or almost over the entire width of the coating machine.
In this way, both the air and the emulsion volume behave like two series-arranged elastic media the softer of which, namely the air, eventually determines the amplitude of the alternating pressure created. At a given frequency and vibration amplitude, the amplitude of this alternating pressure is proportional to the resistance of the medium of sound waves. The resistance of air to sound wave is lower by a factor of 3,600
than that of water, which means that the alternating pressure created is reduced by this factor. Accordingly, the residual-alternating pressure amplitude is three to four times smaller than the static pressure differential governing layer thickness at the coating gap, with the result that it is no longer able to produce any noticeable cross cut in the coating.
The apparatus according to the invention is diagrammatically illustrated by way of Example in the accompanying drawmg.
A roll 5 provides a rotatable support for the substrate to be coated as it passes the coating machine 4. A gap 6 is defined between the substrate supported by the roll 5 and the coating machine 4. A chamber 3 at the inlet end of the machine provides a low pressure at the inlet end of the gap. The coating machine 4 is provided with an internal emulsion chamber 2 which is supplied with coating material as indicated by the arrow in the drawing. A cavity 1, in which a cushion of air is provided, is in communication with the chamber 2.
What we claim is:
1. In an apparatus for coating a layer of viscous material on a movable substrate which includes the combination of a movable substrate, a sealed coating chamber for wetting the substrate, a viscous material for feeding onto said movable substrate, a coating machine for depositing the viscous material on the substrate containing the sealed coating chamber and being operatively associated with the substrate having one end associated with the substrate so as to form a narrow gap between the coating machine and the substrate, the gap having an inlet end at which the substrate enters the gap and an outlet end at which the substrate departs from the gap, and including means in the combination or applying a static pressure differential at a lower pressure at the inlet end and a higher pressure at the outlet end of the narrow gap, and in which the viscous material is fed from the coating machine through an opening from the chamber into the narrow gap, the improvement consisting of a cavity laterally adjoining the said chamber having an opening into the chamber through a chamber sidewall and containing a compressible gas, said gas being encloseable within said cavity by said conveyed viscous material to maintain said static pressure differential and reduce variations in pressure on said feed material.
2. An apparatus as claimed in claim 4, wherein the cavity occupies substantially the entire width of the coating machine.

Claims (1)

  1. 2. An apparatus as claimed in claim 4, wherein the cavity occupies substantially the entire width of the coating machine.
US797809A 1969-02-10 1969-02-10 Apparatus for coating strip-form substrates Expired - Lifetime US3638604A (en)

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4159355A (en) * 1977-11-14 1979-06-26 Scott Paper Company Foam bonding
JPS5624131A (en) * 1979-08-06 1981-03-07 Mitsubishi Rayon Co Ltd Manufacture of thermosetting resin film
US4310295A (en) * 1981-01-28 1982-01-12 E. I. Du Pont De Nemours And Company Device for uniform web pinning
WO1984000016A1 (en) * 1982-06-18 1984-01-05 Hep Products Ab A method for coating a surface with a layer
WO1994023643A1 (en) * 1993-04-12 1994-10-27 Noninvasive Medical Technology Corporation System and method for noninvasive hematocrit monitoring
WO1996011069A1 (en) * 1994-10-06 1996-04-18 Minnesota Mining And Manufacturing Company Tension ascension knife coating method
US5618568A (en) * 1995-02-01 1997-04-08 Extrusion Dies, Inc. Dual-chamber vacuum box

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3067060A (en) * 1959-01-29 1962-12-04 Ulrich Steinemann Ag Ltd Method and apparatus for curtain coating
US3206323A (en) * 1962-06-12 1965-09-14 Eastman Kodak Co Coating high viscosity liquids

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3067060A (en) * 1959-01-29 1962-12-04 Ulrich Steinemann Ag Ltd Method and apparatus for curtain coating
US3206323A (en) * 1962-06-12 1965-09-14 Eastman Kodak Co Coating high viscosity liquids

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4159355A (en) * 1977-11-14 1979-06-26 Scott Paper Company Foam bonding
JPS5624131A (en) * 1979-08-06 1981-03-07 Mitsubishi Rayon Co Ltd Manufacture of thermosetting resin film
JPS6146306B2 (en) * 1979-08-06 1986-10-13 Mitsubishi Rayon Co
US4310295A (en) * 1981-01-28 1982-01-12 E. I. Du Pont De Nemours And Company Device for uniform web pinning
WO1984000016A1 (en) * 1982-06-18 1984-01-05 Hep Products Ab A method for coating a surface with a layer
WO1994023643A1 (en) * 1993-04-12 1994-10-27 Noninvasive Medical Technology Corporation System and method for noninvasive hematocrit monitoring
WO1996011069A1 (en) * 1994-10-06 1996-04-18 Minnesota Mining And Manufacturing Company Tension ascension knife coating method
US5612092A (en) * 1994-10-06 1997-03-18 Minnesota Mining And Manufacturing Company Knife coating method using ascension of the fluid by its tension
CN1090541C (en) * 1994-10-06 2002-09-11 美国3M公司 Tension ascension knife coating method
US5618568A (en) * 1995-02-01 1997-04-08 Extrusion Dies, Inc. Dual-chamber vacuum box

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