WO2021020503A1 - 現像液のリサイクル装置及びリサイクル方法、並びに現像装置 - Google Patents
現像液のリサイクル装置及びリサイクル方法、並びに現像装置 Download PDFInfo
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- WO2021020503A1 WO2021020503A1 PCT/JP2020/029212 JP2020029212W WO2021020503A1 WO 2021020503 A1 WO2021020503 A1 WO 2021020503A1 JP 2020029212 W JP2020029212 W JP 2020029212W WO 2021020503 A1 WO2021020503 A1 WO 2021020503A1
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- rotating body
- developer
- recycling
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- slit
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- G—PHYSICS
- G03—PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
- G03F—PHOTOMECHANICAL PRODUCTION OF TEXTURED OR PATTERNED SURFACES, e.g. FOR PRINTING, FOR PROCESSING OF SEMICONDUCTOR DEVICES; MATERIALS THEREFOR; ORIGINALS THEREFOR; APPARATUS SPECIALLY ADAPTED THEREFOR
- G03F7/00—Photomechanical, e.g. photolithographic, production of textured or patterned surfaces, e.g. printing surfaces; Materials therefor, e.g. comprising photoresists; Apparatus specially adapted therefor
- G03F7/26—Processing photosensitive materials; Apparatus therefor
- G03F7/30—Imagewise removal using liquid means
- G03F7/3092—Recovery of material; Waste processing
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/26—Separation of sediment aided by centrifugal force or centripetal force
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B3/00—Centrifuges with rotary bowls in which solid particles or bodies become separated by centrifugal force and simultaneous sifting or filtering
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- G—PHYSICS
- G03—PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
- G03F—PHOTOMECHANICAL PRODUCTION OF TEXTURED OR PATTERNED SURFACES, e.g. FOR PRINTING, FOR PROCESSING OF SEMICONDUCTOR DEVICES; MATERIALS THEREFOR; ORIGINALS THEREFOR; APPARATUS SPECIALLY ADAPTED THEREFOR
- G03F7/00—Photomechanical, e.g. photolithographic, production of textured or patterned surfaces, e.g. printing surfaces; Materials therefor, e.g. comprising photoresists; Apparatus specially adapted therefor
- G03F7/20—Exposure; Apparatus therefor
- G03F7/2002—Exposure; Apparatus therefor with visible light or UV light, through an original having an opaque pattern on a transparent support, e.g. film printing, projection printing; by reflection of visible or UV light from an original such as a printed image
- G03F7/2012—Exposure; Apparatus therefor with visible light or UV light, through an original having an opaque pattern on a transparent support, e.g. film printing, projection printing; by reflection of visible or UV light from an original such as a printed image using liquid photohardening compositions, e.g. for the production of reliefs such as flexographic plates or stamps
Definitions
- the present invention relates to a developer recycling device for a flexo printing original plate capable of efficiently separating and removing resin agglomerates, a developer recycling method using such a device, and a developing device for a flexographic printing original plate.
- the flexographic printing original plate generally has a structure in which a photosensitive resin layer formed from a photosensitive resin composition is provided on a support.
- Such flexographic printing original plate making is performed, for example, by selectively exposing the photosensitive resin layer with ultraviolet rays and developing the exposed photosensitive resin layer with an aqueous developer.
- the photosensitive resin composition in the photosensitive resin layer in the unexposed portion is removed from the printing plate and dispersed or dissolved in the developing solution.
- the concentration of the photosensitive resin composition dispersed in the developer increases, the development speed decreases, or the photosensitive resin composition dispersed in the developer increases. Aggregates to form floating resin aggregates.
- This resin agglomerate reattaches to the surface of the printing plate and deteriorates the quality of the plate surface. Therefore, it is necessary to discard the developer having a high concentration of the photosensitive resin composition, replace it with a new developer, and restart the plate making. However, it is not preferable from the viewpoint of environmental load and manufacturing cost to repeatedly discard the used developer and replace it with a new developer.
- Patent Document 1 discloses a method of adding a coagulant to a developing solution to positively generate resin agglomerates and removing the resin agglomerates from the developing solution.
- the addition of the coagulant is costly, and there is a problem that the developer to which the coagulant is added cannot be recycled as a developer as it is.
- Patent Document 2 discloses a method of filtering resin agglomerates by circulating operation between a concentration tank and a filtration filter.
- a backwashing treatment a treatment of flowing a filtrate in the direction opposite to the filtration direction
- Patent Documents 3 and 4 disclose a method for separating and removing resin agglomerates using a centrifugal sedimentation type centrifuge having an inside disk. In this method, there is no problem of clogging unlike the separation method using a filter medium, and the developer can be continuously processed up to the limit volume in which resin agglomerates can be accumulated in the centrifuge.
- the inside disk is used in order to prevent the dispersed solid matter having a specific gravity smaller than that of the developing solution from flowing out from the inside to the outside of the rotating portion of the centrifuge.
- Patent Document 3 It is necessary to install it in the centrifuge.
- the inside disc used in Patent Document 3 is fixed and used by screwing or the like, and is troublesome to attach and detach.
- Patent Document 4 discloses an inside disc that does not need to be fixed, but it is troublesome to set optimum conditions in relation to the material of the inside disc to be used, the conditions for centrifugation, and the developing solution.
- it has been difficult to increase the separation / removal ratio of resin agglomerates by the centrifugation method using an inside disk as in Patent Documents 3 and 4. Due to the above-mentioned problems, there has been a demand for a developer recycling device and a recycling method that do not cause clogging or difficulty in setting treatment conditions and have a high separation / removal ratio of resin agglomerates.
- the present invention has been devised in view of the above-mentioned current state of the prior art, and an object of the present invention is to provide a flexographic original plate having a high separation and removal ratio of resin agglomerates without clogging or difficulty in setting treatment conditions. It is an object of the present invention to provide a developer recycling apparatus, a developer recycling method using such an apparatus, and a developing apparatus for a flexographic printing original plate.
- the present inventors provided a slit on the side surface of the rotating body of the centrifuge instead of the inside disk as in Patent Documents 3 and 4, and utilized this slit.
- the present invention has the following configurations (1) to (8).
- It includes a centrifuge having a rotating body for separating resin aggregates from the finished aqueous developer, and the vertical cross-sectional shape including the rotation axis of the rotating body has a substantially cylindrical or substantially conical trapezoidal contour.
- a recycling device wherein the rotating body has a slit on its side surface for allowing the centrifugally separated used aqueous developer to flow out from the inside to the outside of the rotating body.
- the recycling apparatus according to (1) which is in the range of.
- a method comprising separating a resin agglomerate from a used aqueous developer by the recycling apparatus according to any one of.
- resin agglomerates can be efficiently separated and removed from a used developer with a simple structure without using an inside disk.
- FIG. 1 It is sectional drawing which shows one Embodiment of the recycling apparatus of this invention. It is a figure which looked at the part of the rotating body of the centrifuge of the recycling apparatus of FIG. 1 from the top. It is a figure which looked at the part of the rotating body of the centrifuge of the recycling apparatus of FIG. 1 from obliquely above. It is a figure which shows the state in operation of the centrifuge of the recycling apparatus of FIG. It is a figure which shows the overflow situation of the centrifuge of the recycling apparatus of FIG. It is a figure which shows the connection path adopted in an Example.
- Housing 2 Rotating body (main body) 3: Lid-shaped cover of rotating body 4: Slit 5: Rotating shaft (drive shaft) 6: Used developer supply port 7: Treated developer discharge port 8: Non-woven fabric 9: Treated developer 10: Floating component (resin agglutinin) 11: Processed developer 11': Overflowed developer 12: Circulation pump 13: Circulation line 14: Developer tank 15: Flow rate adjustment valve 16: Feed line 17: Open / close valve 18: Centrifuge (recycle) apparatus) 19: Treatment liquid line 20: Treatment liquid tank 21: Inside disk
- the present invention is a device for recycling a used aqueous developer after developing a flexo printing original plate having a photosensitive resin layer by a centrifuge, and centrifuges particularly on the side surface of a rotating body of the centrifuge. It is characterized in that a slit is provided for allowing the used aqueous developer to flow out from the inside to the outside of the rotating body.
- the recycling device of the present invention includes a centrifuge and separates resin agglomerates from a used aqueous developer by a rotating body of the centrifuge.
- the rotating body of the centrifuge has a substantially cylindrical or substantially conical trapezoidal contour in the vertical cross-sectional shape including the rotation axis, but the substantially cylindrical shape conventionally adopted has a point of processing efficiency. Is preferable.
- the resin agglomerates with a light specific gravity contained in the used aqueous developer are supplied to the inside of the rotating body of the centrifuge and centrifuged to become a levitation component on the side close to the rotating body of the rotating body. It collects in and is separated from the remaining aqueous developer.
- the recycling apparatus of the present invention is characterized in that the rotating body has a slit on its side surface for allowing the centrifugally separated used water-based developer to flow out from the inside to the outside of the rotating body.
- This slit has a role of separating the resin agglomerates by centrifugation and allowing the remaining aqueous developer, which is substantially free of the resin agglomerates, to flow out from the inside to the outside of the rotating body.
- this slit makes it possible to efficiently take out a developing solution that does not substantially contain resin agglomerates without providing an inside disk, and it is possible to greatly improve the maintainability of the centrifuge.
- the shape of the slit is not particularly limited, but it is not necessary to provide it continuously (entire surface) as long as the flow of liquid is not significantly reduced, and a divided slit may be used.
- the divided slits include those in which rectangular or circular slits are arranged.
- the slits are preferably provided in parallel with the rotation direction because of ease of manufacture and the flow of treated water.
- the number of slits may be at least one, but when a plurality of slits are provided, it is preferable to arrange the slits on the side surface of the rotating body of the centrifuge so as to be rotationally symmetrical and evenly distributed.
- the method of providing slits on the side surface of the rotating body is not particularly limited.
- the rotating body is formed by dividing the rotating body into upper and lower parts of the lid-shaped cover and the main body, and a continuous slit is provided between the upper and lower divided parts.
- a lid-shaped cover is provided on the upper part of the main body of the rotating body, a spacer having a thickness corresponding to the slit width is partially inserted and fixed with bolts, and the gap between the cover and the main body of the rotating body is continuous. It can be a typical slit.
- a method of forming a continuous slit by attaching the cover of the above is preferable.
- the ratio of the opening area of the slit to the internal volume of the rotating body is within a specific range in order to prevent the slit from being clogged by the resin agglomerates.
- the total opening area opening to the interior of the rotating body of the slit Acm 2, the internal volume of the rotating body when the Bcm 3, the value of the slit opening area ratio (B / A) is 30,000 to The range is preferably in the range of 14000, more preferably in the range of 3500 to 13000. If the slit opening area ratio (B / A) is less than the above lower limit, the removal rate of resin agglomerates may be inferior, and if it exceeds the above upper limit, the treatment efficiency may be inferior.
- the internal volume of the rotating body can be calculated from the diameter and height of the rotating body.
- the number of slits does not matter, and the ratio of the opening area of the slits to the internal volume of the rotating body is important. Even if a large number of small-area slits are formed in a rotating body having the same internal volume or a small number of large-area slits are formed, the same effect can be obtained as long as the total opening areas are the same. Further, the direction of the slit is not particularly limited, and the same effect can be obtained in the horizontal direction, the diagonal direction, the stepped shape, and the shape in which the slit opening area changes.
- the maximum treatment liquid flow rate tends to increase and the removal rate of resin agglomerates tends to decrease.
- the relationship changes when the shape is different. For example, as the diameter of the rotating body increases, the centrifugal force increases, the maximum treatment liquid flow rate increases, and the removal rate of resin agglomerates also tends to increase.
- the opening area of the slit facing the inside of the rotating body is the same as or smaller than the opening area facing the outside of the rotating body.
- the used developer before the treatment is supplied to the rotating body from the supply port and centrifuged.
- the bottom of the rotating body is preferable as the position where the supply port is arranged. Therefore, it is preferable that the slit opening is provided at a position equal to or higher than the center height of the inner wall of the rotating body. Separation performance is better when the slit opening is located far from the developer supply port of the rotating body. This is because the position of the opening of the slit is arranged at a position far from the supply port of the developing solution of the rotating body, so that the used developing solution before processing that has been put into the rotating body is affected by the flow that spreads laterally. This is because the centrifugation process can be performed.
- the centrifuge used in the recycling device of the present invention is a device that generates centrifugal force to separate a solid and a liquid or separate those having different specific gravities.
- the centrifuge used in the present invention preferably centrifuges in the range of centrifuge acceleration of 200 to 4000 G.
- the amount of developer that can be processed by the centrifuge is determined by the volume inside the centrifuge.
- the processing amount is preferably 0.3 liters or more per minute, and when the amount of the developing solution is 200 liters, the processing amount is preferably 1 liter or more per minute.
- a bag made of a non-woven fabric or a resin sheet may be provided along the inner wall of the rotating body of the centrifuge in order to easily take out the resin agglomerates.
- a bag made of a non-woven fabric or a resin sheet along the inner wall of the rotating body, the resin agglomerates accumulated inside the rotating body can be taken out of the rotating body together with the bag made of the non-woven fabric or the resin sheet. it can.
- Nonwoven fabric is more preferable in terms of take-out efficiency.
- the non-woven fabric a commercially available non-woven fabric can be used. In the present invention, it is presumed that by arranging the non-woven fabric so as to cover the inner wall of the rotating body, the developing solution separated from the resin agglomerates by centrifugal force can be easily moved to the liquid flow path through the non-woven fabric.
- the material of the non-woven fabric polyester, polyamide, polyurethane, polyethylene, polypropylene, polyolefin, vinyl chloride, cellulose and the like can be considered, but the material is not limited thereto.
- heat-sealing fibers may be blended within a range that does not interfere with the flow of the treated developer.
- the thickness of the non-woven fabric is preferably 5 mm or more, more preferably 10 mm or more, because if it is too thin, it becomes difficult to stand on its own. On the other hand, if it is too thick, the space for collecting the levitation component is reduced, so 80 mm or less is preferable, and 40 mm or less is more preferable.
- the basis weight of the non-woven fabric if it is too small, the strength of the non-woven fabric is weakened, so 100 g / m 2 or more is preferable, and 200 g / m 2 or more is more preferable. On the other hand, if the basis weight is too large, it interferes with the flow of the liquid, so 800 g / m 2 or less is preferable, and 400 g / m 2 or less is more preferable.
- particularly preferable non-woven fabrics include non-woven fabrics made of materials such as polyethylene, polypropylene, polyester, and cellulose, having a basis weight of 200 to 500 g / m 2 and a thickness of 10 to 30 mm.
- a bag made of a resin sheet a bag made of a resin such as polyethylene can be used.
- the bag made of a resin sheet preferably has fine holes, and may be arranged so as not to obstruct the treated water flow path of the slit.
- the thickness of the resin sheet can be 0.02 to 0.5 mm.
- This developer is a used water-based developer after developing a flexographic printing master plate having a photosensitive resin layer containing a water-dispersible synthetic rubber-based polymer.
- the used developer contains resin aggregates derived from the constituents of the photosensitive resin layer in the unexposed portion of the flexographic printing master plate.
- a water-dispersible polymer is used as the synthetic rubber-based polymer which is a main component of the photosensitive resin layer. Therefore, the resin agglomerates of the used developer contain a large amount of water-dispersible synthetic rubber-based polymer. Since these water-dispersible synthetic rubber-based polymers have a lighter specific gravity than water, they become floating components by centrifugation and can be easily separated from the remaining water-based developer.
- the water-dispersible synthetic rubber-based polymer is used to impart appropriate rubber elasticity to the photosensitive resin layer, and conventionally known rubber components can be used.
- the water-dispersible synthetic rubber-based polymer is preferably solid at room temperature in order to impart rubber elasticity.
- Specific examples of water-dispersible synthetic rubber-based polymers include polybutadiene, polychloroprene, polyacrylonitrile-butadiene, polyacrylic, epichlorohydrin, polyurethane, polyisoprene, polystyrene isoprene copolymer, and polystyrene-butadiene copolymer.
- Examples thereof include coalescence, methyl methacrylate-butadiene copolymer, ethylene-propylene copolymer, butyl polymer, chlorinated polyethylene, etc., which can be obtained by copolymerizing these polymers with other components such as acrylic acid and methacrylic acid. Polymers and the like can be mentioned.
- the water-dispersed latex may be a latex having a crosslinked structure represented by the degree of gelation in the molecule.
- the latex having a crosslinked structure in the molecule is preferably a hydrophobic polymer obtained from an aqueous dispersion latex having a weight average gelation degree of 20 to 80%. These may be used alone or in combination of two or more.
- the water-dispersible latex is one in which the polymer fine particles of rubber are dispersed in water to form a stable suspension. A polymer is obtained by removing water from this water-dispersed latex.
- the photosensitive resin layer of the flexographic printing original plate may contain a water-insoluble synthetic rubber-based polymer within a range that does not adversely affect the performance in order to improve physical properties and water resistance.
- a water-insoluble synthetic rubber-based polymer examples include polybutadiene, polychloroprene, polyacrylonitrile-butadiene, polyurethane, polyisoprene, polystyrene-isoprene copolymer, and polystyrene-butadiene copolymer.
- the photosensitive resin layer of the flexographic printing original plate may contain a water-soluble or water-dispersible polymer other than the water-dispersible synthetic rubber-based polymer.
- water-soluble or water-dispersible polymer include water-soluble polyamides in which hydrophilic groups are introduced into polyamides, water-dispersible polyamides, partially saponified polyvinyl acetate and derivatives thereof, and anionic acrylic polymers.
- the water-dispersible synthetic rubber-based polymer is dispersed in the developer, so that the polymer concentration in the developer suddenly increases. It will not rise. Further, since the synthetic rubber polymer is water-dispersible, it is suitable for waste liquid treatment by centrifugation.
- the photosensitive resin composition of the flexo printing original plate contains, in addition to the above-mentioned water-dispersible synthetic rubber-based polymer, a photopolymerizable unsaturated monomer compound, a photopolymerization initiator and the like. These additional components are well known to those of skill in the art and will not be described in detail here.
- the flexographic printing original plate has a support in addition to the photosensitive resin layer, and the photosensitive resin layer can be arranged on the support. Further, a protective layer and an infrared sensitive layer can be arranged on the photosensitive resin layer.
- the developing solution to be processed by the recycling apparatus of the present invention is a water-based developing solution containing water as a main component.
- the aqueous developer may be water alone or an aqueous solution to which a water-soluble development accelerator is added.
- the development accelerator include surfactants, acids, bases, salts and the like.
- the surfactant include a cationic surfactant, an anionic surfactant, and a nonionic surfactant.
- the acid include inorganic acids such as sulfuric acid, nitric acid and phosphoric acid, and organic acids such as formic acid, acetic acid, oxalic acid, succinic acid, citric acid, maleic acid and paratoluenesulfonic acid.
- Examples of the base include lithium hydroxide, sodium hydroxide, potassium hydroxide, calcium hydroxide and the like.
- Examples of the salt include sodium carbonate and sodium silicate. From the viewpoint of development speed, a development accelerator that is soluble in water is preferable. As the development accelerator, a commercially available soap or detergent may be used. As the development accelerator, a surfactant, an acid, a base, and a salt may be used in combination, and the optimum formulation of the development accelerator may be determined according to the components of the photosensitive resin composition.
- the aqueous developer may contain an organic solvent soluble in water in addition to water.
- organic solvent examples include methanol, ethanol, isopropyl alcohol, cellosolve, glycerin, ethylene glycol, polyethylene glycol and the like.
- an antifoaming agent may be added to the aqueous developer in order to suppress the generation of bubbles.
- the defoaming agent may be any water-soluble defoaming agent. Examples of the components of the defoaming agent include higher alcohols, fatty acid derivatives, silica, alumite, silicone and the like.
- FIG. 1 is a schematic view of an embodiment of the recycling device of the present invention.
- 1 is a housing
- 2 is a rotating body
- 3 is a lid-shaped cover of the rotating body
- 4 is a slit formed between the rotating body 2 and the lid-shaped cover 3.
- 5 is the rotation shaft (drive shaft) of the rotating body
- 6 is the supply port of the used developing liquid to be processed
- 7 is the discharge port of the processed development liquid
- 8 is.
- a non-woven fabric installed so as to cover the inner wall of the rotating body 2 all around.
- the rotating body 2 has a substantially cylindrical contour in the vertical cross-sectional shape including the rotating shaft 5 of the rotating body.
- the used developer supplied from the supply port 6 is a resin aggregate having a small specific gravity in the rotating body 2 of the centrifuge and a treated developer having a large specific gravity from which the resin aggregate has been removed. Is separated into.
- the rotating body 2 has a basket-shaped main body as shown in FIGS. 2 and 3, and a donut-shaped lid-shaped cover 3 is mounted on the basket-shaped main body, and a gap (slit 4) is provided between the main body and the cover. I put a spacer in order to open it and screwed it in 4 places.
- the rotating body is connected to the motor through a rotating shaft (drive shaft), and an outward centrifugal force is generated by the centripetal acceleration generated when the rotating body is rotated.
- the used developer is supplied into the rotating body from the supply port, and as soon as it is supplied into the rotating body, it sticks to the side surface of the rotating body, and due to centrifugal force, a resin having a small specific gravity as shown in FIG. It is separated into a floating component 10 composed of agglomerates and a treated developer 9 having a large specific gravity.
- the water-dispersible synthetic rubber-based polymer derived from the photosensitive resin layer of the unexposed portion of the printing original plate has a lighter specific gravity than water, so that it becomes a floating component 10 and becomes the inside of the rotating body (center side). ), And the treated developer 9 having a large specific gravity is separated to the outside of the rotating body (the inner wall side of the rotating body). Water pressure is applied to the inner wall of the rotating body by centrifugal force, and the treated developer 9 having a large specific gravity on the inner wall side of the rotating body flows out from the slit 4.
- the outflowing liquid has a shape of being spray-like because it passes through the slit by the force of water pressure.
- the spouted developing solution is collected in the housing 1 shown in FIG. 1 and guided to the discharge port 7.
- the treated developer discharged from the discharge port can be used as a recycled developer because the resin agglomerates have been removed.
- the resin agglomerates 10 are accumulated on the non-woven fabric.
- a phenomenon occurs in which the treated developer 11'overflows over the lid-shaped cover 3 on the upper part of the rotating body.
- the supply of the developer is stopped before the overflow occurs, the rotation of the centrifuge is stopped after the dehydration operation for a while, and the non-woven fabric is taken out to discharge the resin agglomerates.
- a new non-woven fabric may be placed to restart the centrifugation.
- bolt joining between the rotating body and the lid-shaped cover of the rotating body is used as an example, but a method other than bolt joining is also possible.
- the rotating body and the lid-shaped cover are integrated, and there is no problem even if the slit is cut. Further, even if there are many holes instead of slits, the same effect can be obtained.
- the rotating body of the centrifuge has been described by taking a vertical structure as an example, but a horizontal structure has the same effect.
- the recycling apparatus of the present invention can be suitably used as an effective alternative to the conventional recycling apparatus in a conventionally known flexographic printing original plate developing apparatus equipped with a developer recycling apparatus.
- Photosensitive Resin Composition A 91 parts by mass of butadiene latex (manufactured by Nippon Zeon, LX111NF solid content concentration 55%) as a water-dispersible synthetic rubber polymer, oligobutadiene acrylate (manufactured by Kyoeisha Chemical Co., Ltd.
- ABU-3 molecular weight as a photopolymerizable unsaturated monomeric compound 2700) 15 parts by mass, 10 parts by mass of lauryl methacrylate, 10 parts by mass of trimethylpropantrimethacrylate, 1 part by mass of benzyl dimethyl ketal as a photopolymerization initiator, and PFT-3 (urethane urea structure) manufactured by Kyoeisha Chemical Co., Ltd. as a hydrophilic polymer.
- Photosensitive resin composition B 56.4 parts by mass of butadiene latex (manufactured by Nippon Zeon, LX111NF solid content concentration 55%) as an water-dispersible synthetic rubber-based polymer, and polybutadiene-terminated diacrylate (manufactured by Osaka Organic Chemistry, Ltd.) as a photopolymerizable unsaturated monomer compound. 10 parts by mass of BAC-45) and 10 parts by mass of acrylic monomer (1,9-nonanediol dimethacrylate) were mixed, and the water content was evaporated in a dryer heated to 120 ° C. for 2 hours to obtain a mixture.
- Photosensitive resin composition C 100 parts by mass of carboxy-modified methyl methacrylate-butadiene latex (manufactured by Nippon A & L, MR174 solid content concentration 50%) as a water-dispersible synthetic rubber polymer, oligobutadiene acrylate as a photopolymerizable unsaturated monomeric compound (manufactured by Kyoeisha Chemical Co., Ltd.)
- ABU-3 Molecular weight 2700) 15 parts by mass, lauryl methacrylate 10 parts by mass, trimethylpropantrimethacrylate 10 parts by mass, benzyl dimethyl ketal as a photopolymerization initiator 1 part by mass, PFT-3 manufactured by Kyoeisha Chemical Co., Ltd.
- hydrophilic polymer Polymer having a urethane urea structure with a molecular weight of about 20,000, solid content concentration 25%
- 20 parts by mass 20 parts by mass, 0.1 part by mass of hydroquinone monomethyl ether as a polymerization inhibitor, 9 parts by mass of liquid butadiene as a plasticizer, 5 parts by mass of toluene
- the mixture was kneaded at 105 ° C. using a pressurized kneader, and then toluene and water were distilled off under reduced pressure to obtain a photosensitive resin composition C.
- Photosensitive resin composition D 71 parts by mass of styrene-butadiene latex (manufactured by Nippon Zeon, C4850 solid content concentration 70%) as an water-dispersible synthetic rubber polymer, and oligobutadiene acrylate (manufactured by Kyoeisha Chemical Co., Ltd. ABU-) as a photopolymerizable unsaturated monomeric compound.
- styrene-butadiene latex manufactured by Nippon Zeon, C4850 solid content concentration 70%
- oligobutadiene acrylate manufactured by Kyoeisha Chemical Co., Ltd. ABU-
- the infrared-sensitive layer coating solution prepared in (3) is applied using an appropriate type of bar coater, and the temperature is 120 ° C. After drying for 5 minutes, an infrared sensitive layer having a film thickness of 1.5 ⁇ m was laminated on the PET film. The optical density at this time was 2.3. This optical density was measured by a black-and-white transmission densitometer DM-520 (Dainippon Screen Mfg. Co., Ltd.).
- the protective layer coating solution prepared in (2) is applied onto the infrared sensitive layer using an appropriate type of bar coater, dried at 120 ° C. for 5 minutes, and the film thickness is 1 on the PET film.
- a laminated film was obtained in which a 5.5 ⁇ m infrared sensitive layer and a 0.5 ⁇ m film thickness protective layer were laminated in this order.
- a developer tank 14 for storing 50 L of the aqueous developer, a circulation pump 12 for circulating the developer in the tank, a flow rate adjusting valve 15, a centrifuge 18, and a treatment liquid tank 20 were connected as shown in FIG.
- ⁇ Measurement method of NV value representing non-volatile content> The centrifuge, the developer tank, and the treatment liquid tank are connected by the above connection method, and the developer prepared according to the method for producing the used aqueous developer is subjected to a predetermined centrifuge acceleration by the centrifuge. It was treated by centrifugation at the number of revolutions. The treated developer collects in the developer tank.
- the liquid sampled from here was used as a sample after treatment, and the liquid sampled from the developer tank before treatment was used as a sample before treatment. Two grams of each of the pre-treatment sample and the post-treatment sample were taken in an aluminum foil cup and dried in a vacuum dryer at 80 ° C.
- NV value [%] (mass after drying-mass of aluminum foil cup) ⁇ (mass before drying-mass of aluminum foil cup) x 100
- Example 1 Using the photosensitive resin printing original plate A, a used water-based developer was prepared according to the method for preparing a used water-based developer.
- a non-woven fabric (made of polyester, thickness 20 mm, grain 380 g / m 2 ) (FIGS. 1 and 2) was provided.
- the total A of the opening areas of the slits was adjusted by inserting a spacer having a thickness of 0.03 mm between the lid-shaped cover of the rotating body and the main body of the rotating body and screwing the lid-shaped cover of the rotating body.
- This centrifuge is connected to the developing tank and the processing liquid tank by the above connection method, the flow rate is measured, the centrifuge is operated, and when the developing solution in an amount twice the capacity of the rotating body is passed, overflow ( The flow rate at which FIG. 5) does not occur was set as the maximum processing amount.
- the resin agglutination removal rate was evaluated by the above method after stopping when a developer having twice the volume of the rotating body was passed through at this maximum processing amount. The results are shown in Table 1.
- Examples 14-16 Centrifugation treatment was performed in the same manner as in Example 1 except that the photosensitive resin printing original plate B, C, or D was used instead of the photosensitive resin printing original plate A. The results are shown in Table 2.
- Examples 1 and 2 are examples in which the slit opening area ratio is in a particularly preferable range, and the resin agglutination recovery rate and the maximum processing capacity are good.
- Example 3 since the diameter of the cylindrical rotating body is larger than that in Example 1, the centrifugal force applied to the treatment liquid is large, and the resin agglutination removal rate is further improved.
- Example 4 since the slit opening area ratio is smaller than that in Example 3, the resin agglutination removal rate is lowered, but the maximum processing flow rate is increased.
- Example 5 From Example 5, it can be seen that good centrifugation can be performed even when the slit position is not above the cylindrical rotating body but at the center. From Examples 6 to 7, it can be seen that even if the centrifuge acceleration is increased or decreased as compared with Example 1, sufficient centrifugation is possible within the acceleration region of a normal centrifuge.
- Example 8 is an example in which the non-woven fabric is not used, but the result is as good as in Example 1, and it is good even if the non-woven fabric is not used (although it is inconvenient in terms of taking out the resin agglomerates). It can be seen that the centrifugation treatment is possible. In Example 9, since the slit opening is below the cylindrical rotating body as shown in FIG.
- Example 12 has a structure in which there are four slits as shown in FIG.
- the thirteenth embodiment has a structure in which there are 18 slit openings as shown in FIG.
- the number of openings was different in the same manner as in Example 12. Specifically, 18 grooves having a depth of 0.4 mm and a width of 4 mm were previously formed in the upper part of the cylindrical rotating body so as to form an opening between the cylindrical rotating body and the lid-shaped cover. Even if the number of slits is changed in this way, the diameter of the cylindrical rotating body and the value of the slit opening area ratio do not change as compared with the first embodiment, so that the same evaluation result is obtained. Further, as shown in Table 2, even in Examples 14 to 16 in which the type of the photosensitive resin printing original plate (photosensitive resin layer) was changed, good treatment results were obtained as in Example 1.
- Comparative Example 1 since the slit opening area ratio is too large than the preferable range, the maximum processing amount is small. In Comparative Example 2, since the slit opening area ratio is smaller than the preferable range, the resin removal rate is small.
- Comparative Example 3 as shown in FIG. 14, the inside disk 21 was placed inside the cylindrical rotating body and centrifuged. The inside disc was made of a polypropylene plate having a thickness of 0.3 mm, and was fixed to the inside of the cylindrical rotating body at the position shown in FIG. 14 with an upper lid and four bolts. In this method, since convection occurs in the rotating cylinder, the resin agglutination removal rate is low and the separation efficiency is inferior. In Comparative Example 4, as shown in FIG.
- resin agglomerates can be efficiently separated and removed from a used developer with a simple structure without using an inside disk. Therefore, the present invention is extremely useful in the art.
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Abstract
Description
(1)水分散性の合成ゴム系重合体を含有する感光性樹脂層を有するフレキソ印刷原版を現像した後の使用済の水系現像液をリサイクルするための装置であって、前記装置が、使用済の水系現像液から樹脂凝集物を分離するための回転体を有する遠心分離機を含み、前記回転体の回転軸を含む鉛直方向の断面形状が、略円筒形又は略円錐台形の輪郭を有し、前記回転体が、その側面に、遠心分離された使用済水系現像液を前記回転体の内側から外側に流出させるためのスリットを有することを特徴とするリサイクル装置。
(2)前記スリットの前記回転体の内部に開く開口面積の合計をAcm2、前記回転体の内部体積をBcm3とした場合に、スリット開口面積比率(B/A)の値が30000~140000の範囲であることを特徴とする(1)に記載のリサイクル装置。
(3)前記回転体が、上下に分割されて構成され、それらの上下の分割体の間に前記スリットが形成されていることを特徴とする(1)又は(2)に記載のリサイクル装置。
(4)前記スリットの開口が、前記回転体の内壁の中央高さ以上の位置に設けられていることを特徴とする(1)~(3)のいずれかに記載のリサイクル装置。
(5)前記回転体の内壁を覆うように樹脂凝集物を収集するための不織布又は樹脂製シート製の袋が設置されていることを特徴とする(1)~(4)のいずれかに記載のリサイクル装置。
(6)前記水分散性の合成ゴム系重合体が、ブタジエン骨格及び/又はスチレン骨格を有することを特徴とする(1)~(5)のいずれかに記載のリサイクル装置。
(7)水分散性の合成ゴム系重合体を含有する感光性樹脂層を有するフレキソ印刷原版を現像した後の使用済の水系現像液をリサイクルする方法であって、(1)~(6)のいずれかに記載のリサイクル装置によって、使用済の水系現像液から樹脂凝集物を分離することを含むことを特徴とする方法。
(8)水分散性の合成ゴム系重合体を含有する感光性樹脂層を有するフレキソ印刷原版を、リサイクル水系現像液を含む水系現像液を用いて現像するためのフレキソ印刷原版の現像装置であって、前記現像装置が、現像後の使用済の水系現像液をリサイクルするために(1)~(6)のいずれかに記載のリサイクル装置を含むことを特徴とするフレキソ印刷原版の現像装置。
2:回転体(本体)
3:回転体の蓋状カバー
4:スリット
5:回転軸(駆動軸)
6:使用済の現像液の供給口
7:処理済の現像液の排出口
8:不織布
9:処理済の現像液
10:浮上成分(樹脂凝集物)
11:処理済の現像液
11´:オーバーフローした処理済の現像液
12:循環ポンプ
13:循環ライン
14:現像液タンク
15:流量調整バルブ
16:送りライン
17:開閉バルブ
18:遠心分離機(リサイクル装置)
19:処理液ライン
20:処理液タンク
21:インサイドディスク
図1は、本発明のリサイクル装置の一実施形態の概略図である。図1中、1は、ハウジングであり、2は、回転体であり、3は、回転体の蓋状カバーであり、4は、回転体2と蓋状カバー3の間に形成されたスリットであり、5は、回転体の回転軸(駆動軸)であり、6は、処理される使用済の現像液の供給口であり、7は、処理済の現像液の排出口であり、8は、回転体2の内壁を一周覆うように設置された不織布である。
(1)感光性樹脂組成物の作製
感光性樹脂組成物A:
水分散性の合成ゴム系重合体としてブタジエンラテックス(日本ゼオン製、LX111NF 固形分濃度55%)91質量部、光重合性不飽和単量体化合物としてオリゴブタジエンアクリレート(共栄社化学製ABU-3:分子量2700)15質量部、ラウリルメタクリレート10質量部、トリメチロールプロパントリメタクリレート10質量部、光重合開始剤としてベンジルジメチルケタール1質量部、親水性重合体として共栄社化学製のPFT-3(ウレタンウレア構造を有する分子量約20,000の重合物、固形分濃度25%)20質量部、重合禁止剤としてハイドロキノンモノメチルエーテル0.1質量部、可塑剤として液状ブタジエン9質量部をトルエン5質量部とともに容器中で混合してから、加圧ニーダーを用いて105℃で混練りし、その後トルエンと水を減圧留去して、感光性樹脂組成物Aを得た。
水分散性の合成ゴム系重合体としてブタジエンラテックス(日本ゼオン製、LX111NF 固形分濃度55%)56.4質量部、光重合性不飽和単量体化合物としてポリブタジエン末端ジアクリレート(大阪有機化学製、BAC-45)10質量部と、アクリルモノマー(1,9-ノナンジオールジメタクリレート)10質量部とを混合し、120℃に加熱した乾燥機で2時間水分を蒸発させて、混合物を得た。この混合物と、ブタジエンゴム(日本ゼオン製、ニポールBR1220)6質量部と、界面活性剤(日油製、ノニオンTA-405)7質量部(固形分として4質量部)と、可塑剤として液状ブタジエン10質量部とをニーダー中で45分間混練した。その後、ニーダー中に、重合禁止剤としてハイドロキノンモノメチルエーテル0.2質量部と、光重合開始剤としてベンジルジメチルケタール1質量部とを投入し、5分間混練して、感光性樹脂組成物Bを得た。
水分散性の合成ゴム系重合体としてカルボキシ変性メチルメタクリレート-ブタジエンラテックス(日本エイアンドエル製、MR174 固形分濃度 50%)100質量部、光重合性不飽和単量体化合物としてオリゴブタジエンアクリレート(共栄社化学製ABU-3:分子量2700)15質量部、ラウリルメタクリレート10質量部、トリメチロールプロパントリメタクリレート10質量部、光重合開始剤としてベンジルジメチルケタール1質量部、親水性重合体として共栄社化学製のPFT-3(ウレタンウレア構造を有する分子量約20,000の重合物、固形分濃度25%)20質量部、重合禁止剤としてハイドロキノンモノメチルエーテル0.1質量部、可塑剤として液状ブタジエン9質量部をトルエン5質量部とともに容器中で混合してから、加圧ニーダーを用いて105℃で混練りし、その後トルエンと水を減圧留去して、感光性樹脂組成物Cを得た。
水分散性の合成ゴム系重合体として、スチレン-ブタジエンラテックス(日本ゼオン製、C4850 固形分濃度 70%)71質量部、光重合性不飽和単量体化合物としてオリゴブタジエンアクリレート(共栄社化学製ABU-3:分子量2700)15質量部、ラウリルメタクリレート10質量部、トリメチロールプロパントリメタクリレート10質量部、光重合開始剤としてベンジルジメチルケタール1質量部、親水性重合体として共栄社化学製のPFT-3(ウレタンウレア構造を有する分子量約20,000の重合物、固形分濃度25%)20質量部、重合禁止剤としてハイドロキノンモノメチルエーテル0.1質量部、可塑剤として液状ブタジエン9質量部をトルエン5質量部とともに容器中で混合してから、加圧ニーダーを用いて105℃で混練りし、その後トルエンと水を減圧留去して、感光性樹脂組成物Dを得た。
低ケン化度ポリビニルアルコール(PVA405 (株)クラレ製)と可塑剤(サンフレックスSE270 三洋化成工業製 脂肪族多価アルコール系ポリエーテルポリオール 固形分濃度85%)とNBRラテックス(SX1503A 日本ゼオン(株)製 固形分濃度42%)を、固形分重量比で35/35/30になるように、水・イソプロピルアルコール混合液に溶解し、保護層塗工液を調製した。
カーボンブラック分散液(AMBK-8 オリエント化学工業(株)製)と共重合ポリアミド(PA223 東洋紡績(株)製)を固形分重量比で63/37になるように、メタノール・エタノール・イソプロピルアルコール混合液に溶解し、感赤外線層塗工液を調製した。
両面に離形処理を施した100μmのPETフィルム上に、(3)で調製した感赤外線層塗工液を適切な種類のバーコーターを用いて塗工し、120℃で5分間乾燥し、PETフィルム上に膜厚1.5μmの感赤外線層を積層した。この時の光学濃度は2.3であった。この光学濃度は白黒透過濃度計DM-520(大日本スクリーン製造(株))によって測定した。次いで、上記感赤外線層の上に、(2)で調製した保護層塗工液を適切な種類のバーコーターを用いて塗工し、120℃で5分間乾燥し、PETフィルム上に膜厚1.5μmの感赤外線層と膜厚0.5μmの保護層がこの順に積層されている積層フィルムを得た。
共重合ポリエステル系接着剤を塗工した100μmのPETフィルム上に、(1)で作製した感光性樹脂組成物Aを配置し、その上から、(4)で作製した積層フィルムを重ね合わせた。ヒートプレス機を用いて100℃でラミネートし、PET支持体、接着層、感光性樹脂層、保護層、感赤外線層および離型処理PET保護フィルム(カバーフィルム)からなるフレキソ印刷原版を得た。版の総厚は1.14mmであった。感光性樹脂組成物AをB,C,又はDに変更した以外は、感光性樹脂印刷原版Aと同様にして、感光性樹脂印刷原版B~Dを作製した。
水道水中に、現像促進剤としてのオレイン酸ナトリウムを現像液全体の1質量%の量で溶解し、水系現像液を作成した。この水系現像液中で、カバーフィルムを剥離した上記フレキソ印刷原版を、直径200μmのナイロン製フィラメントを毛材としたブラシでこする方式の現像機で現像することで、フレキソ印刷原版を現像した後の使用済の水系現像液を調製した。このとき、水系現像液中の感光性樹脂組成物の濃度が5質量%となるようにした。
上記水系現像液50Lを溜める現像液タンク14とこのタンク内の現像液を循環させる循環ポンプ12、流量調整バルブ15、遠心分離機18、処理液タンク20を図6のように接続した。
遠心分離機と現像液タンク、処理液タンクを上記接続方法で接続して、上記使用済の水系現像液の作製方法の通りに調製した現像液を、遠心分離機で所定の向心加速度となる回転数で遠心分離して処理した。処理済の現像液は処理液タンクに溜まる。ここからサンプリングした液を処理後サンプルとし、処理前に現像液タンクからサンプリングした液を処理前サンプルとした。アルミホイル製カップに処理前サンプルと処理後サンプルをそれぞれ2グラム取り、真空乾燥機で80℃で2時間乾燥させて、不揮発分を表すNV値[%]を測定した。質量の測定は電子精密天秤で行った。計算式は以下の通りである。
NV値[%]=(乾燥後質量-アルミホイル製カップの質量)÷(乾燥前質量-アルミホイル製カップの質量)×100
測定したNV値から樹脂濃度を理論計算して求めた。計算式は以下の通りである。
樹脂濃度[%]=NV値-オレイン酸ナトリウムの添加量(1質量%)
処理前サンプルと処理後サンプルの樹脂濃度から樹脂凝集物除去率を計算した。計算式は以下の通りである。
樹脂凝集物除去率[%]=(処理前サンプルの樹脂濃度-処理後サンプルの樹脂濃度)÷(処理前サンプルの樹脂濃度)×100
遠心分離機と現像液タンク、処理液タンクを上記接続方法で接続して、流量調整バルブを開き、遠心分離機の排出口から処理済の現像液を留出させた。留出する処理済の現像液を10秒間カップで受けて、メスシリンダーにてカップで受けた容量[L]を計測した。容量計測値の6倍を1分間当たりの流量[L/min]とした。
感光性樹脂印刷原版Aを使用して、使用済の水系現像液の調製方法に従って使用済の水系現像液を調製した。図7に示した遠心分離機〔円筒形の回転体の内部直径R=30cm、円筒形の回転体の高さH=20cm、底部密閉型〕の回転体の内部に、内壁を一周覆うように不織布(ポリエステル製、厚み20mm、目付380g/m2)(図1、図2)を設けた。回転体の蓋状カバー状カバーと回転体の本体の間で、0.03mmの厚みのスペーサーを入れて回転体の蓋状カバーをねじ止めすることでスリットの開口面積の合計Aを調整した。この遠心分離機を前記接続方法で現像タンク、処理液タンクと接続し、流量を測定してから遠心分離機を運転して、回転体容量の2倍量の現像液を通液したところでオーバーフロー(図5)が発生しない流量を最大処理量とした。この最大処理量で回転体容量の2倍量の現像液を通液したところで止めて、上記方法で樹脂凝集物除去率を評価した。その結果を表1に示す。
遠心分離機の構造や遠心分離条件を表1に示すように変更した以外は、実施例1と同様の方法で実験を行った。その結果を表1に示す。
感光性樹脂印刷原版Aの代わりに感光性樹脂印刷原版B,C,又はDを使用した以外は、実施例1と同様の方法で遠心分離処理を行った。その結果を表2に示す。
具体的には、実施例1、2は、スリット開口面積比率が特に好ましい範囲である例であり、樹脂凝集物回収率及び最大処理能力が良好になっている。
実施例3は、実施例1と比べて円筒形回転体の直径が大きいため、処理液にかかる遠心力が大きくなり、樹脂凝集物除去率がさらに良好になっている。
実施例4は、実施例3に比べてスリット開口面積比率が小さいため、樹脂凝集物除去率が下がるが、最大処理流量が増大している。
実施例5から、スリット位置が円筒形回転体の上方ではなく中央部であっても、良好な遠心分離処理が可能であることが分かる。
実施例6~7から、実施例1と比べて向心加速度を増加又は減少させても、通常の遠心分離機の加速度領域内であれば十分な遠心分離が可能であることが分かる。
実施例8は、不織布を使用していない例であるが、実施例1と同様に良好な結果であり、不織布を使用しなくとも(樹脂凝集物の取り出しの点では不便であるが)良好な遠心分離処理が可能であることが分かる。
実施例9は、図9に示すようにスリット開口部が円筒形回転体の下方にあるため、実施例1と比べて樹脂除去率が若干低下しているが、依然としてスリットにより良好な遠心分離が可能となっている。
実施例10は、図10に示すように円筒形の回転体の代わりに円錐台形の回転体を使用したものである。実施例1と比較すると樹脂凝集物除去率がわずかに低下するが、このような形状でも良好な結果である。
実施例11は、図11に示すようにスリットの断面を斜めとし、円筒形回転体本体の上部をすり鉢状としたものである。すり鉢の傾斜角度は、水平方向から30度になるようにした。このような形状でも、実施例1と変わらず良好な結果となっている。
実施例12は、図12に示すようにスリットが4カ所あるような構造である。実施例1などのようなスペーサーを入れることで円筒形回転体の蓋状カバーと円筒形回転体の本体の間に連続的な隙間を作る方法ではなく、スペーサーは入れないで、予め円筒形回転体の上部に深さ0.7mm幅10mmの溝を4カ所入れて、円筒形回転体の蓋状カバーとの間に開口部ができるような構造とした。このようにスリットの個数を変更しても、実施例1と比較して円筒形回転体の直径もスリット開口面積比率の値も変わらないため、同様の評価結果となっている。
実施例13は、図13に示すようにスリット開口部が18カ所あるような構造である。実施例12と同様の方法で開口部の数を異ならせた。具体的には、予め円筒形回転体の上部に深さ0.4mm幅4mmの溝を18カ所入れて、円筒形回転体蓋状カバーとの間に開口部ができるような構造とした。このようにスリットの個数を変更しても、実施例1と比較して円筒形回転体の直径もスリット開口面積比率の値も変わらないため、同様の評価結果となっている。
さらに、表2に示されるように、感光性樹脂印刷原版(感光性樹脂層)の種類を変更した実施例14~16においても、実施例1と同様に良好な処理結果であった。
比較例2は、スリット開口面積比率が好ましい範囲よりも小さいため、樹脂除去率が小さい。
比較例3は、図14に示すようにインサイドディスク21を円筒形回転体の内側に設置して遠心分離を実施した。インサイドディスクは厚み0.3mmのポリプロピレン製の板で作成し、円筒形回転体の内側の図14で示した位置に、上蓋と4つのボルトで固定した。この方式では、回転筒内の対流が発生するため、樹脂凝集物除去率が低く、分離効率に劣る。
比較例4では、図15に示すようにスペーサーを入れないことでスリットを全く設けずに遠心分離した。この場合、図5に示すようなオーバーフローによって処理済の現像液を取り出すため、遠心力により浮上して内側に溜まった樹脂凝集物が処理済の現像液と一緒に流出してしまい、ほとんど樹脂凝集物が分離できていない。
Claims (8)
- 水分散性の合成ゴム系重合体を含有する感光性樹脂層を有するフレキソ印刷原版を現像した後の使用済の水系現像液をリサイクルするための装置であって、前記装置が、使用済の水系現像液から樹脂凝集物を分離するための回転体を有する遠心分離機を含み、前記回転体の回転軸を含む鉛直方向の断面形状が、略円筒形又は略円錐台形の輪郭を有し、前記回転体が、その側面に、遠心分離された使用済水系現像液を前記回転体の内側から外側に流出させるためのスリットを有することを特徴とするリサイクル装置。
- 前記スリットの前記回転体の内部に開く開口面積の合計をAcm2、前記回転体の内部体積をBcm3とした場合に、スリット開口面積比率(B/A)の値が30000~140000の範囲であることを特徴とする請求項1に記載のリサイクル装置。
- 前記回転体が、上下に分割されて構成され、それらの上下の分割体の間に前記スリットが形成されていることを特徴とする請求項1又は2に記載のリサイクル装置。
- 前記スリットの開口が、前記回転体の内壁の中央高さ以上の位置に設けられていることを特徴とする請求項1~3のいずれかに記載のリサイクル装置。
- 前記回転体の内壁を覆うように樹脂凝集物を収集するための不織布又は樹脂製シート製の袋が設置されていることを特徴とする請求項1~4のいずれかに記載のリサイクル装置。
- 前記水分散性の合成ゴム系重合体が、ブタジエン骨格及び/又はスチレン骨格を有することを特徴とする請求項1~5のいずれかに記載のリサイクル装置。
- 水分散性の合成ゴム系重合体を含有する感光性樹脂層を有するフレキソ印刷原版を現像した後の使用済の水系現像液をリサイクルする方法であって、請求項1~6のいずれかに記載のリサイクル装置によって、使用済の水系現像液から樹脂凝集物を分離することを含むことを特徴とする方法。
- 水分散性の合成ゴム系重合体を含有する感光性樹脂層を有するフレキソ印刷原版を、リサイクル水系現像液を含む水系現像液を用いて現像するためのフレキソ印刷原版の現像装置であって、前記現像装置が、現像後の使用済の水系現像液をリサイクルするために請求項1~6のいずれかに記載のリサイクル装置を含むことを特徴とするフレキソ印刷原版の現像装置。
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| EP20847436.1A EP4009105A4 (en) | 2019-08-01 | 2020-07-30 | Recycling device and recycling method for developing liquid, and development device |
| CN202080055660.3A CN114207528B (zh) | 2019-08-01 | 2020-07-30 | 显影液的回收装置及回收方法和显影装置 |
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| WO2023032747A1 (ja) * | 2021-08-31 | 2023-03-09 | 富士フイルム株式会社 | 再生処理装置、洗い出し装置、及びフレキソ印刷版の製造方法 |
| JP2023087940A (ja) * | 2021-12-14 | 2023-06-26 | 東京応化工業株式会社 | 金属レジスト除去用洗浄液、及び該洗浄液を用いた洗浄方法 |
| US12428737B2 (en) | 2021-12-14 | 2025-09-30 | Tokyo Ohka Kogyo Co., Ltd. | Cleaning liquid used for cleaning metal resists, and cleaning method using cleaning liquid |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| NL2034187B1 (en) * | 2023-02-20 | 2024-09-03 | Xsys Germany Gmbh | System and methods for developing a relief precursor to obtain a relief structure |
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| JPWO2021020503A1 (ja) | 2021-09-13 |
| EP4009105A4 (en) | 2023-08-30 |
| CN114207528B (zh) | 2025-04-15 |
| EP4009105A1 (en) | 2022-06-08 |
| CN114207528A (zh) | 2022-03-18 |
| US20220252987A1 (en) | 2022-08-11 |
| JP6826787B1 (ja) | 2021-02-10 |
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