Process for the manufacture of photopolymer plates

• US 5,135,827 A
• Filed: 02/13/1991
• Issued: 08/04/1992
• Est. Priority Date: 02/14/1990
• Status: Expired due to Term

• Current Assignee: E. I. du Pont de Nemours and Company (Corteva, Inc.)
• Original Assignee: Hoechst Aktiengesellschaft (Sanofi )
• Inventors: Bohm, Dieter, Faust, Raimund-Josef, Petry, Rudolf, Schlosser, Hans-Joachim, Gersdorf, Joachim
• Primary Examiner(s): Hamilton, Cynthia
• Application Number:
  US07/654,578
• Time in Patent Office: 538 Days
• Field of Search: 430/306, 430/309, 430/327, 430/286, 430/270, 430/281, 430/935, 430/30, 430/271, 430/330, 430/287
• US Class Current: 430/30
• CPC Class Codes: B29C 2035/0833 using actinic light
• CPC Class Codes: B29C 31/04 Feeding of the material to be moulded, e.g. into a mould cavity B29C39/08 takes precedence; using a material distribution system to two or more fixed injection moulds B29C45/125
• CPC Class Codes: B29C 43/24 Calendering
• CPC Class Codes: B29C 48/37 Gear pumps
• CPC Class Codes: B29C 48/395 using screws surrounded by a cooperating barrel, e.g. single screw extruders
• CPC Class Codes: G03F 7/16 Coating processes; Apparatus therefor applying coatings to base materials in general B05; applying photosensitive compositions to base for photographic purposes G03C1/74
• CPC Class Codes: Y10S 430/136 Coating process making radiation sensitive element

Abstract

A continuous process for the manufacture of photopolymer plates having a precise and constant thickness in which the components of the photopolymer layer are melted in a screw extruder, the melt is conveyed to the sheet die by means of a gear pump and then into a roll gap of a calender, wherein the melt leaving the sheet die does not form a rotating bead in the calender gap downstream therefrom. The photopolymer plates prepared in this manner have high homogeneity of the components of the photopolymerizable mixture, have a highly precise and constant thickness, are transparent, do not tend to form specks and guarantee a long shelf life.

Claims

1. A continuous process for the manufacture of photopolymer plates, comprising the steps of:

(a) introducing into a screw extruder a photopolymerizable mixture comprising at least one thermoplastic elastomeric polymer, at least one ethylenically mono- or poly-unsaturated compound which can be polymerized by free radicals and has a boiling point of more than about 100°

C. at atmospheric pressure and at least one compound capable of initiating polymerization of said unsaturated compound upon exposure to actinic light;

(b) melting and degassing said mixture in said extruder to form a melt;

(c) metering said melt into a sheet die; and

then

(d) conveying said melt into a roll gap of a two-roll calender at such a rate that substantially no rotating bead is formed in said roll gap.

2. A process according to claim 1, wherein step (c) comprises transporting said melt to said sheet die via a melt metering pump.

3. A process according to claim 2, wherein said melt metering pump comprises a spur-toothed gear pump.

4. A process according to claim 2, wherein the rotational speed of the rolls of said two-roll calender and the speed of said metering pump are controlled in such a manner that substantially no rotating bead is formed.

5. A process according to claim 4, further comprising measuring the pressure in said sheet die and controlling the rotational speed of the rolls of said two-roll calender in relation thereto such that substantially no rotating bead is formed.

6. A process according to claim 1, wherein said screw extruder comprises a self-cleaning twin-screw extruder.

7. A process according to claim 1, wherein said screw extruder comprises a kneading block, a toothed block, at least one opening for the metering in of said mixture, at least one degassing section and a discharge opening.

8. A process according to claim 7, wherein step (a) comprises metering solid components of said mixture into a first feed opening of an unheated first section of said extruder and metering liquid components of said mixture into at least one second feed opening of at least one subsequent heated section of said extruder.

9. A process according to claim 1, further comprising premixing the components of said photopolymerizable mixture prior to introducing said components into said extruder.

10. A process according to claim 9, wherein said premixing is effected in a ploughshare, ribbon, paddle, drum or free-falling mixer.

11. A process according to claim 10, wherein a powder which is insoluble in the liquid components of said mixture and has an average particle size of about 0.005 to 50 μ

m is admixed to the premixture, and said thermoplastic polymer is used in the form of granules.

12. A process according to claim 1, further comprising heating at least one section of said extruder to an average temperature of about 100°

to 220°

C.

13. A process according to claim 12, wherein said heated section is at a temperature of about 130°

to 170°

C.

14. A process according to claim 7, further comprising heating said degassing section to a temperature of about 60°

to 140°

C.

15. A process according to claim 1, wherein the overall screw length of said extruder is about 5 to 50 times the screw diameter.

16. A process according to claim 15, wherein the overall screw length of said extruder is about 10 to 40 times the screw diameter.

17. A process according to claim 1, wherein the gap width of said sheet die is about 1.2 to 50 times the calender gap width.

18. A process according to claim 17, wherein the gap width of said sheet die is about 1.5 to 50 times the calender gap width.

19. A process according to claim 1, further comprising a step (e) of applying at least one layer to the photopolymer layer produced in said calender to form a multi-layer element.

20. A process according to claim 19, wherein step (e) is effected by carrying a film on each roll of said calender as they rotate.

21. A process according to claim 1, wherein the product sheet produced in said calender gap leaves said calender gap at an angle of about 90°

relative to the connecting line between the axes of said calender rolls.

22. A process according to claim 21, further comprising transporting said product sheet produced in said calender gap by means of a first take-off belt.

23. A process according to claim 22, wherein said first take-off belt comprises a nonperforated take-off belt.

24. A process according to claim 22, further comprising cooling concurrently the top and bottom of said product sheet.

25. A process according to claim 22, further comprising additionally transporting said product sheet by means of a perforated second take-off belt.

26. A process according to claim 25, further comprising applying a vacuum to said product sheet so as to secure said product sheet on said belt.

27. A process according to claim 22, further comprising partially exposing the bottom surface of said product sheet during said transporting.