WO2009123363A1 - フィルム状触媒の製造方法 - Google Patents
フィルム状触媒の製造方法 Download PDFInfo
- Publication number
- WO2009123363A1 WO2009123363A1 PCT/JP2009/057298 JP2009057298W WO2009123363A1 WO 2009123363 A1 WO2009123363 A1 WO 2009123363A1 JP 2009057298 W JP2009057298 W JP 2009057298W WO 2009123363 A1 WO2009123363 A1 WO 2009123363A1
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- WO
- WIPO (PCT)
- Prior art keywords
- catalyst
- film
- protective material
- bending
- gears
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/064—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof containing iron group metals, noble metals or copper
- B01J29/072—Iron group metals or copper
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J33/00—Protection of catalysts, e.g. by coating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/56—Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional [3D] monoliths
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/58—Fabrics or filaments
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0215—Coating
- B01J37/0219—Coating the coating containing organic compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0215—Coating
- B01J37/0225—Coating of metal substrates
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B21—MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
- B21D—WORKING OR PROCESSING OF SHEET METAL OR METAL TUBES, RODS OR PROFILES WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
- B21D13/00—Corrugating sheet metal, rods or profiles; Bending sheet metal, rods or profiles into wave form
- B21D13/04—Corrugating sheet metal, rods or profiles; Bending sheet metal, rods or profiles into wave form by rolling
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- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C26/00—Coating not provided for in groups C23C2/00 - C23C24/00
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T156/00—Adhesive bonding and miscellaneous chemical manufacture
- Y10T156/11—Methods of delaminating, per se; i.e., separating at bonding face
- Y10T156/1168—Gripping and pulling work apart during delaminating
- Y10T156/1195—Delaminating from release surface
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/19—Sheets or webs edge spliced or joined
- Y10T428/192—Sheets or webs coplanar
- Y10T428/193—Double faced corrugated sheets or webs connected
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/28—Web or sheet containing structurally defined element or component and having an adhesive outermost layer
- Y10T428/2835—Web or sheet containing structurally defined element or component and having an adhesive outermost layer including moisture or waterproof component
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/28—Web or sheet containing structurally defined element or component and having an adhesive outermost layer
- Y10T428/2848—Three or more layers
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
- Y10T428/2913—Rod, strand, filament or fiber
- Y10T428/2933—Coated or with bond, impregnation or core
- Y10T428/294—Coated or with bond, impregnation or core including metal or compound thereof [excluding glass, ceramic and asbestos]
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T442/00—Fabric [woven, knitted, or nonwoven textile or cloth, etc.]
- Y10T442/30—Woven fabric [i.e., woven strand or strip material]
- Y10T442/3382—Including a free metal or alloy constituent
- Y10T442/3415—Preformed metallic film or foil or sheet [film or foil or sheet had structural integrity prior to association with the woven fabric]
Definitions
- the present invention relates to a method for producing a film catalyst suitable as a catalyst for gas-liquid reaction.
- a film catalyst in which a catalyst is supported on a film substrate is known (WO 2 0 0 5/0 3 5 1 2 2).
- this film-like catalyst is sometimes processed and formed into a honeycomb shape in the form of a corrugation.
- the catalyst layer carried on the base material is wrinkled by contact with the forming tool. There is a problem that it may occur or, in some cases, the catalyst may fall off partially.
- JP-A 8-1 4 1 3 9 3 a metal base material having a catalyst layer was sandwiched between flexible plate-like members, and then passed between a pair of synthetic resin gears to form a corrugated shape. Thereafter, a method of heating a metal substrate is described, and it is described that a catalyst body is processed by sandwiching a high-quality paper as a flexible plate-like member with a polyethylene resin.
- a plate-shaped member When such a plate-shaped member is used, the stress acting on the catalyst layer cannot be sufficiently relaxed in the meshing space between the gears, and the catalyst layer may be damaged. Further, in the space for meshing between the gears, the pressure applied to the catalyst layer and the plate-like member increases, so that stress is applied to the synthetic resin gear and the durability of the gear is impaired. Also travel If wrinkles occur in the plate-like member at times, the total thickness of the plate-like member substantially increases at the wrinkled portion, so a very large stress is applied to the catalyst layer, and mechanical destruction of the catalyst layer cannot be avoided.
- JP-A 2000-1 898 14 describes a method of press molding with a molding apparatus using a mold for thermoforming a catalyst coated body in which a catalyst component is coated on an inorganic fiber or a net-like body.
- a molding apparatus is described in which a flexible porous layer is provided on the surface of a mold.
- the present invention comprises a step of forming a catalyst layer on one or both sides of a support to produce a film-like catalyst, and a step of bending the film-like catalyst.
- a bending tool two gears disposed so as to face each other are used as a bending tool, and between the catalyst layer of the film catalyst and the two gears.
- This is a method for producing a film-like catalyst, in which bending processing is performed with a protective material having a compression ratio of 40 to 95% interposed therebetween.
- the ratio (t 2 ti) of the thickness of the film-like catalyst (t and the total thickness (t 2 ) of the protective material is 4 to 20; And the relationship between t 2 and t 2 is t, ⁇ T ⁇ tt 2 where T is a combination of the gears of the two gears. The distance between the gears, with the distance close to the shortest distance as the zero reference.
- the present invention comprises a step of forming a catalyst layer on one or both sides of a support to produce a film-like catalyst, and a step of pressing and bending the film-like catalyst.
- the bending tool includes two upper and lower plate-shaped bending tools, and the two plate-shaped bending tools have corrugated teeth on a flat plate, The concave and convex portions of the corrugated teeth are arranged so as to overlap with each other.
- the catalyst layer of the film catalyst and the bent portion are bent.
- JP—A 2 0 0 0— 1 8 9 8 1 4 suppresses the wear of the mold metal itself.
- the surface porous layer provided on the mold should have strength and durability. It was difficult. When stress is applied to the mold and the porous layer during molding, stress is concentrated at the interface, causing separation between the porous layer and the mold. Therefore, it was difficult to fix it permanently, that is, it was difficult to have durability in molding use.
- the porous layer has a high friction coefficient, which causes problems such as damage to the catalyst body due to the frictional force applied to the catalyst body.
- the present invention provides a method for producing a film catalyst that can be processed into a desired shape without damaging the catalyst layer.
- a film catalyst processed into a desired shape can be obtained without damaging the catalyst layer.
- the method for producing a film catalyst of the present invention is used as a catalyst for various organic synthesis reactions. It can be used as a method for producing a film catalyst.
- the protective material preferably has a dynamic friction coefficient of 0.05 to 0.25, or the protective material is a nonwoven fabric.
- a catalyst layer is formed on one surface or both surfaces of a long support to manufacture a long film catalyst.
- the first production method is suitable for processing a long film-shaped catalyst, but can also be applied to processing a film-shaped catalyst of each desired shape.
- the coating composition used for the production of a long film catalyst can be prepared as follows.
- a catalyst active material or a catalyst in which a catalyst active material is supported on a porous material can be used as the powdered catalyst contained in the coating composition.
- the catalyst active material may be any component that is effective for the applied chemical reaction,
- the porous material is a catalyst carrier that supports the catalytic active material.
- the porous material include activated carbon, alumina, silica, zeolite, titania, silica-alumina, and diatomaceous earth. Can be preferably used.
- a porous material having a high surface area can be used, and a molecular sieve or the like can also be used.
- the powdered catalyst preferably has an average particle size of 0.001 to 500 / zm, more preferably 0.5 to 150 mm, and even more preferably 1 to 50 m. A sharp distribution is preferred.
- the specific surface area by BET method is preferably 1 to 500 m 2 / g, more preferably 5 to 200 mVg, and still more preferably 10 to 100 m 2 / g.
- the content of the powdered catalyst in the solid content (100% by mass) in the coating composition is preferably 60 to 90% by mass, more preferably 60 to 85% by mass, and still more preferably 70 to 90% by mass. 8 5% by mass.
- the binder used in the coating composition is preferably one that is excellent in binding properties between the powdered catalysts and the support surface, withstands the reaction environment, and does not adversely affect the reaction system.
- binders include cellulose resins such as carboxymethylcellulose hydroxyethyl cellulose, fluorine resins such as polytetrafluoroethylene and polyvinylidene fluoride, polyvinyl alcohol, urethane resins, epoxy resins, polyamide resins, and polyimides.
- thermoplastic resins and thermosetting resins such as resins, polyamide-imide resins, polyester resins, phenol resins, melamine resins, and silicone resins are used.
- thermosetting resins such as phenolic resin, furan resin, and epoxy resin are preferable, and more preferable at the time of curing.
- a thermosetting resin accompanied by a condensation reaction can be used.
- thermosetting resin When a thermosetting resin is used as the binder, the strength of the coating film and the binding property are improved by improving the crosslinking density by the curing reaction, and the catalytic activity of the powdered catalyst is increased by making the catalyst coating film porous by the condensation reaction. It can be pulled out effectively.
- a preferred combination of a powdered catalyst and a binder when the film-like catalyst obtained by the production method of this step is used in a reaction for producing a tertiary amine from alcohol and primary amine or secondary amine, A combination of monoruthenium ternary powder catalyst and phenol resin can be mentioned.
- the binder content in the solid content (100% by mass) in the coating composition is preferably 10 to 40% by mass, more preferably 15 to 40% by mass, and still more preferably 15 to 30% by mass.
- the content ratio of the powdered catalyst and the binder within the predetermined range, it becomes possible to control the degree of exposure of the powdered catalyst, and further, the catalytic activity ability inherent in the powdered catalyst is increased. It can be pulled out and the catalyst layer can be removed easily.
- the content of the binder 1 in the solid content is 40% by mass or less, the thickness of the binder covering the surface of the powder catalyst or the coverage by the binder becomes appropriate, and the catalytic activity of the powder catalyst is sufficient. As a result, high catalytic activity can be exhibited.
- the blending ratio of the binder in the solid content is 10% by mass or more, the catalytic activity is sufficiently developed, and the binding force between the powder catalysts or between the powder catalyst supports is improved, and the film catalyst.
- the amount of catalyst layer separation and partial dropout during the manufacturing process and reaction operation is suppressed
- a solvent is used to improve the wettability of the powdered catalyst surface, dissolve the binder, and promote mixing and homogenization of these blends. Any solvent may be used as long as it does not adversely affect the catalytic activity of the powdered catalyst, and various water-soluble or water-insoluble solvents can be selected depending on the type of binder used.
- the pore structure of the film-like catalyst can be controlled by selecting one of these.
- the solvent preferably has good binder solubility, and may be used in combination of two or more solvents, and the pore structure of the catalyst layer can be changed by selecting a solvent suitable for the binder used. Can be controlled.
- Solvents include water; alcohols such as methyl alcohol, ethyl alcohol, isopropyl alcohol, butyl alcohol, and aryl alcohol; ketones such as acetone, methyl ethyl ketone (MEK), and methyl isobutyl ketone (MIBK); Diols or derivatives thereof such as monol, propylene glycol, diethylene glycol, polyethylene glycol, polypropylene glycol, diethylene glycol monoethyl ether, polypropylene glycol monoethyl ether, polyethylene glycol monoallyl ether, polypropylene glycol monoallyl ether; Glycerol or its derivatives such as glycerol monoethyl ether, glyceryl monoallyl ether; Ethers such as lofuran and dioxane; liquid paraffin, decane, decene, methylnaphthalene, decalin, kerosene, diphenylmethane, toluene
- the coating composition may contain a surfactant or a cutting agent as a dispersion aid, an inorganic particle, a fibrous material, etc. as an aggregate, and a high boiling point solvent as a porosity aid. it can.
- the coupling agent has an effect of improving physical properties by performing molecular crosslinking at the interface between the inorganic filler and the organic polymer matrix.
- coupling agents those commonly known as silane coupling agents, titanate coupling agents and aluminate coupling agents can be used, and a combination of multiple force coupling agents may be used to adjust the concentration. It may be used after diluting with a compatible organic solvent.
- the fibrous substance organic fiber or inorganic fiber is used.
- organic fibers examples include polyamide nylon 6, nylon 6 nylon fiber, polypinyl alcohol fiber, polyester polyethylene terephthalate, polybutylene terephthalate fiber, polyarylate fiber, polyvinylidene chloride, poly Examples thereof include vinyl chloride-based, polyacrylonitrile-based, and polyolefin-based polyethylene and polypropylene fibers.
- the organic fibers include organic regenerated fibers, and examples thereof include cellulose-based rayon and acetate.
- inorganic fiber Glass fiber, carbon fiber, activated carbon fiber, ceramic fiber, etc. can be used. By blending each of the fibers, the mechanical strength of the catalyst layer can be improved due to the manifestation of the aggregate effect.
- the preparation of the coating composition is not particularly limited as long as each component can be uniformly mixed, but in the present invention, it is preferably prepared using a media type mill or a pent shaker.
- a media-type mill By using a media-type mill, it is possible to uniformly treat each component of the coating composition described above from its structure and mechanism. Therefore, by controlling the particle size and dispersion state of the powdered catalyst, It is suitable for controlling the pore size distribution of the catalyst layer of the film catalyst.
- media type mills ball mills, trials, AD mills, twin AD mills, basket mills, twin basket mills, handy mills, daren mills, dynomils, apex mills, suyuichi mills, pisco mills, sand grinders and beads were used.
- a dissolver-type mixing and dispersing machine can be used as a dispersing machine other than the media type mill.
- the solid content in the coating composition is preferably 10 to 80% by mass because the pore structure is controlled at the time of desorption of the solvent from the formed catalyst layer and affects the formation of the pore structure. More preferably, it is 20-70 mass%, More preferably, it is 25-65 mass%.
- the viscosity of the coating composition is selected within a preferable range depending on the coating method, and is, for example, 5 to 10,000 mPas, preferably 20 to 5000 mPas, more preferably 50 to l OOOmPas.
- the coating composition is applied to a long support and formed into a film to produce a catalyst intermediate. Then, it can be dried (cured) at room temperature.
- the coating method conventionally known methods can be used, and various coating methods such as blade, roll, knife, bar, spray, dip, spin, comma, kiss, gravure, and die coating can be exemplified.
- the formation of the magnetic layer on the support can be performed by using PDV, CVD, etc. in addition to coating.
- the film-like catalyst preferably has a catalyst layer thickness of 500 m or less, more preferably 100 Aim or less, and even more preferably 50 in or less. Also, catalyst loading per unit area, 0. 5 ⁇ 1 0 0 g Zni 2 is preferred,.
- the support used in the present invention is long or sheet-like, and the length and width are not particularly limited, and the thickness is preferably 1 mm or less.
- the material include copper foil, stainless steel foil, and aluminum foil.
- copper foil and stainless steel foil can be used from the viewpoint of workability and corrosion resistance.
- the surface of the support is preferably subjected to a roughening treatment or a force pulling treatment from the viewpoint of improving the adhesion to the catalyst layer.
- the coupling agent described above can be used, and preferably the same kind as that used for preparing the paint can be used.
- the drying and curing processes are intended to remove the solvent and unreacted monomers contained in the coating composition after coating and film formation on the support.
- the heating temperature and the heating time are adjusted according to the composition of the coating composition.
- the curing reaction can also be allowed to proceed.
- the drying and curing process is preferably performed in an atmosphere heated with an inert gas such as air, water vapor, nitrogen, argon, or the like, or a method of spraying such a heat medium is used.
- radiant heat such as infrared rays or far infrared rays is used.
- Various methods such as a method of heating, a heating method using an induced conductive current by electromagnetic waves can be used, a method combining these methods, or a method of natural drying at room temperature (air drying) can also be used.
- Components desorbed in this step are a volatile component mainly composed of a solvent and a hardening reaction product.
- the volatile components other than the solvent include unreacted monomer components.
- the drying and curing conditions must be adjusted according to the physical properties of the volatile components, mainly the binder and solvent contained in the coating composition.
- the catalyst layer can be selected by selecting the solvent and setting the drying and curing conditions.
- the porous structure (pore volume) can be controlled.
- the pore structure becomes smaller as the drying temperature is lower and the drying air volume is smaller.
- volatile components mainly solvents
- the drying and curing treatment employs a drying method and drying conditions that do not adversely affect the catalytic activity inherent in the powdered catalyst used in the present invention.
- a hot air drying process is used to obtain the desired film catalyst.
- the typical drying and curing conditions are 60 to 400, preferably 70 to 25, more preferably 80 to: at a temperature of L 50, preferably 0.5 to 3 O mZ. It is desirable to carry out the drying and curing treatment at a wind speed of sec, more preferably 1 to 2 O mZ sec, preferably 1 second or more, more preferably 10 minutes or more, and even more preferably 30 minutes or more. In the case where only drying without a curing reaction is intended, it is preferable to dry the coating composition immediately after applying the coating composition to the support. By adjusting the drying conditions at this time, the porosity of the coating film You can control the structure.
- the time from the formation of the catalyst layer on the support to the elimination of the volatile components mainly composed of the solvent is shorter, preferably within 2 hours, more preferably within 30 minutes, and further. Preferably within 5 minutes.
- the binder contains a thermosetting resin
- the catalyst intermediate is shaped with the uncured product remaining in the catalyst layer obtained by coating and drying (prepolymer state), and then finally heated. It is desirable to process.
- the drying and curing treatment of the catalyst intermediate performed before the final heat treatment may be terminated in a state where an uncured product remains in the thermosetting resin. It is partly cured until handling at the time of shape processing can be performed, and it is desirable that the retention and mechanical strength of the catalyst layer be improved compared to the time of film formation.
- the drying before the final heat treatment for obtaining the target film-like catalyst is typically from 60 to 400, preferably from 70 to 25, more preferably, by hot air drying. 80-: at a temperature of L 50, preferably more than 0.5-3 O m / se It is desirable to perform the drying treatment at a wind speed of 1 to 2 O mZ sec, preferably for 0.5 to 300 seconds, more preferably for 1 to 100 seconds. Step of bending a long film catalyst> Next, this step will be described with reference to FIG. FIG. 1 is a conceptual diagram for explaining this process.
- a long film catalyst 10 produced in the previous process is wound on the delivery roll 1 and is sequentially delivered in the direction of the arrow from the delivery roll 1.
- a catalyst layer is formed on one or both sides of the long film catalyst 10.
- the protective rolls 11 are wound around the delivery rolls 2 and 3, and are sent out in parallel with the delivery of the long film catalyst 10 from the delivery roll 1.
- the protective material 11 may be one sheet, but may be two or more layers. When two or more sheets are stacked, slip occurs between the two protective members existing between the gears 15 and 16 during bending, and the frictional force applied to the film catalyst is reduced. In addition, since a gap is formed between the two protective materials, the apparent compression rate increases, which is preferable in that the stress applied to the film-like catalyst during bending can be reduced. As shown in FIG. 1, the protective material 11 sent from the delivery roll 3 is changed in the delivery direction in the middle by using the support roll 4.
- the protective material 11 in contact with the catalyst layer may be sent out, or both protective materials 1 1 may be sent out.
- the delivery speed of delivery roll 1 and delivery rolls 2 and 3 are the same, or delivery roll 1 is faster. For example, it can be in the range of 0.5 to 5 O mZm in.
- the protective material 11 has the same width as the long film catalyst 10 or a slightly larger width, and the thickness (t,) of the long film catalyst 10 And the total thickness of the protective material 1 1 (t 2 ) t 2 t! 4 to 20 is preferable, and 4 to 12 is more preferable.
- the thickness (t,) is the total thickness of the catalyst layer (when there are catalyst layers on both sides of the support, the support thickness, the total thickness of one catalyst layer and the other catalyst layer).
- Thickness (t 2 ) is the total thickness of the protective material used in the bending process (if there are catalyst layers on both sides of the support, this is the total thickness of the two protective materials, and two more on each side of the support In the case of bending, the total thickness of the four protective materials).
- the protective material 11 has a compressibility measured by the method described in the examples of 40 to 95%, preferably 50 to 95%, more preferably 70 to 95%. It is.
- the protective material 11 preferably has a dynamic friction coefficient of 0.05 to 0.25, more preferably 0.05 to 0.2, and still more preferably 0.1 to 0.2.
- the protective material 11 preferably has a porosity of 50% or more, more preferably 80 to 98%, and still more preferably 90 to 98%. By setting the porosity to the above range, the protective material itself can be easily compressed and deformed.
- the protective material used in the present invention has voids from the viewpoint of exhibiting such an action.
- the protective material 11 is preferably made of a non-woven fabric, and the material of the non-woven fabric is not particularly limited.
- the protective material 11 is made of a single fiber material such as known PET, PE, PP, or contains two or more types of fiber materials. Or having a core-sheath structure can be used.
- the long film-like catalyst 10 is passed between two gears 15 and 16 that are arranged to face each other with the teeth sandwiched between the protective materials 1 1 from both sides. . At this time, one protective material 11 is positioned between each of the two gears 15 and 16 and the long film catalyst 10.
- the two gears 15 and 16 can be made of metal such as iron or stainless steel.
- gears 15 and 16 are used in this way, bending work is less than when using gears with synthetic resin teeth, such as JP-A 8 _ 1 4 1 3 9 3.
- a spur gear can be used as the gears 15 and 16, and the circular pitch (the value obtained by dividing the circumferential length of the gear pitch circle by the number of teeth) is 2 to 20 mm. It is possible to process with l ⁇ 20 mm.
- the long film-like catalyst 10 0 'processed into a wave shape is an extrusion action by two gears 15 and 16
- the two protective members 1 1 are pushed out by the take-up rolls 2 'and 3', respectively.
- a film catalyst for example, square
- a method of bending by inserting a square film catalyst one by one between the two gears 15 and 16 sending out It is possible to apply a method in which a rectangular film catalyst is placed on the protective material 11 sent from the roll 2 or is temporarily placed and temporarily bent and placed and bent. In this method, the cutting process is not necessary.
- T is the inter-gear distance when the convex portion and concave portion of the two gears are held together and the distance between the two gears is reduced to the shortest distance as the zero reference.
- the long film catalyst 1 0 'processed into a wave shape in the previous process has the desired shape and After being cut into large sizes, for example, as shown in FIG. 3, it can be used as a catalyst assembly 20 in which a plurality of sheets are combined.
- the manufacturing method of this embodiment is a method of pressing one by one.
- the film-like catalyst can be produced in the same manner as in the first production method, and can be prepared in advance in a desired shape and size. Therefore, a long film can be used in the first production method. There is no need for a post-process cutting step as in the case of using a catalyst.
- two plate-shaped bending tools placed opposite each other are used.
- the two plate-shaped bending tools are made of metal, an upper bending tool having a corrugated tooth formed on a flat plate, and a corrugated concave portion and a convex portion of the upper bending tool on the flat plate.
- It consists of a lower bending tool having convex and concave corrugated teeth.
- a protective material on the corrugated teeth of the lower bending tool, place a film-shaped catalyst of the desired shape (having a catalyst layer on both sides or one side), and then place it on it.
- protective material is put into protective material.
- the film catalyst is pressed through the protective material to obtain a film catalyst processed into a wave shape. It is also possible to apply a method of pressing by placing two bending tools on the left and right. Since the protective material is the same as that of the first manufacturing method described above, the catalyst layer of the film-like catalyst is prevented from being damaged during the bending process.
- the film-like catalyst obtained by the production method of this step can be used depending on the type of the catalyst. Although it can be used as a catalyst for organic synthesis reactions, it can be applied to gas phase, liquid phase, and liquid reaction system. For example, oxidation of olefin, oxidation of alcohol, isomerism of olefin , Isomerization of aromatics, carbonylation, hydrogenation of ester, preferably dehydrogenation reaction, hydrogenation reaction.
- the combination of copper-nickel-ruthenium ternary powder catalyst and phenol resin as binder is used in combination with alcohols with dehydrogenation and hydrogenation reactions and primary or secondary amines to tertiary. Suitable for reactions for producing amines.
- FIG. 1 is a conceptual diagram for explaining a production method of the present invention.
- FIG. 2 is a partially enlarged view for explaining the gear spacing shown in FIG.
- FIG. 3 is a perspective view of a catalyst assembly using a film catalyst obtained by the production method of the present invention.
- the present invention has been described based on the preferred embodiments, the present invention is not limited to the above embodiments. The following examples describe the practice of the present invention. The examples are illustrative of the invention and are not intended to limit the invention.
- T. is the thickness of the specimen at a load of 49 Pa
- T D is the thickness to the test at a maximum load of 59 kPa
- a 20 cm X 20 cm test piece was prepared and attached to the test table of the measuring device.
- the contact surface of the contact was pressed against the specimen with a force of 49 cN, and the specimen was moved 2 cm horizontally at a constant speed of 0.1 cmZsec.
- the specimen was given a uniaxial tension of 19.6 c NZcm.
- the thickness of the protective material was measured by a method in accordance with JIS L 1096.
- the probe diameter was 25.2 mm
- the load was 0.343 N
- the measurement pressure was 0.7 kPa.
- a 10% by mass aqueous sodium carbonate solution was gradually added dropwise while controlling the pH to 9-10. After aging for 1 hour, the precipitate was filtered, washed with water, dried at 80 ° for 10 hours, and calcined at 60 ° for 3 hours to obtain a powdered catalyst.
- the proportion of metal oxide was 50% by mass
- the proportion of synthetic zeolite was 50% by mass.
- a wide-mouth polyethylene bottle was set in a paint shaker and mixed and dispersed for 30 minutes to obtain a coating composition.
- the coating composition was applied to both sides of the copper foil with a comma coater.
- treatment was carried out at 100 ° C. for 120 seconds, and then a film catalyst was obtained.
- the thickness of the catalyst layer was 50 m on one side, and the total thickness combined with the copper foil was 140 m.
- the catalyst layer had a supported amount of 63 g / m 2 per side, and the supported amount of the powdery catalyst was 47 g / nre per side.
- Protective material 1 Nonwoven fabric made of PE (sheath) ZP ET (core) (basis weight 20 g / m 2 ) made by melt-blowing method
- Protective material 2 Spunbond non-woven fabric Ecule 3151A (basis weight 15 gZm 2 ) protection manufactured by Toyobo Material 3: Mitsui Chemicals spunbond nonwoven fabric Syntex PS104 (basis weight 20gZm 2 )
- Protective material 4 Spunbond nonwoven fabric Elves S1003WDO (basis weight lOOgZm 2 )
- Protective material 5 100% cotton woven fabric ( Basis weight 144 ⁇ 111 2 )
- Protective material 6 Toyobo spunbond nonwoven fabric ECLURE 3A01A (basis weight lOOgZm 2 )
- Protective material 7 Mitsui Chemicals spunbond nonwoven fabric Syntex PS120 (basis weight lOOgZm 2 )
- Protective material 8 Japan Paper-made PPC paper recycled cut plate 100N (
- Protective material 1 1 Pile sheet made of PTFE fiber (raised height 2 thighs, basis weight 5 10g / m 2 )
- Protective material 1 2 Twill weave fabric made of PTFE fiber (Toyoflon manufactured by Toray Industries, Inc.) 466g / m 2 )
- Protective material 1 3 Silicone rubber sheet (basis weight 654g / m 2 , thickness 0.55mm)
- Protective material 14 PET film (basis weight 45g / m 2 , thickness 0.03mm)
- ⁇ Processing test (1)> The surface of the film-like catalyst processed into a corrugated sheet and the surface of the catalyst material before processing are visually observed.
- ⁇ Processing test (2)> A comparative observation of the surface of the film catalyst when the protective material is processed into a corrugated sheet with wrinkles generated and the surface of the catalyst material before processing. These were evaluated according to the following criteria. In addition, the situation during ⁇ Processing Test (1)> was evaluated for running conditions.
- the thickness (ti) of the film catalyst is the total thickness of the support thickness plus both S catalysts.
- the gears 15 and 16 used in the machining were of the same shape, and those with a circular pitch of 4 mm and tooth depth of 2.5 mm were used.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Crystallography & Structural Chemistry (AREA)
- Catalysts (AREA)
Abstract
Description
Claims
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP09727047.4A EP2260941B1 (en) | 2008-04-04 | 2009-04-03 | Method for manufacturing a film-shaped catalyst |
| ES09727047.4T ES2605238T3 (es) | 2008-04-04 | 2009-04-03 | Método para la fabricación de un catalizador laminado |
| US12/935,948 US8501665B2 (en) | 2008-04-04 | 2009-04-03 | Method for manufacturing film catalyst |
| CN2009801123487A CN101990465B (zh) | 2008-04-04 | 2009-04-03 | 薄膜状催化剂的制造方法 |
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2008-098333 | 2008-04-04 | ||
| JP2008098333 | 2008-04-04 | ||
| JP2009-084049 | 2009-03-31 | ||
| JP2009084049A JP5449823B2 (ja) | 2008-04-04 | 2009-03-31 | フィルム状触媒の製造方法 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2009123363A1 true WO2009123363A1 (ja) | 2009-10-08 |
Family
ID=41135706
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2009/057298 Ceased WO2009123363A1 (ja) | 2008-04-04 | 2009-04-03 | フィルム状触媒の製造方法 |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US8501665B2 (ja) |
| EP (1) | EP2260941B1 (ja) |
| JP (1) | JP5449823B2 (ja) |
| CN (1) | CN101990465B (ja) |
| ES (1) | ES2605238T3 (ja) |
| WO (1) | WO2009123363A1 (ja) |
Families Citing this family (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE112011104476B4 (de) | 2010-12-21 | 2015-06-18 | Kao Corporation | Verfahren zur Erzeugung eines tertiären Amins |
| DE112011104474T5 (de) | 2010-12-21 | 2013-09-19 | Kao Corp. | Säulen-Kontaktanlage und Verfahren für ihren Betrieb |
| ES2592530T3 (es) | 2011-06-17 | 2016-11-30 | Fiberweb, Llc | Artículo de múltiples capas permeable al vapor, sustancialmente impermeable al agua |
| CN103747955B (zh) | 2011-06-23 | 2017-03-22 | 纤维网公司 | 可透蒸气而基本不可透水的多层制品 |
| WO2012178027A2 (en) | 2011-06-23 | 2012-12-27 | Fiberweb, Inc. | Vapor-permeable, substantially water-impermeable multilayer article |
| US9765459B2 (en) | 2011-06-24 | 2017-09-19 | Fiberweb, Llc | Vapor-permeable, substantially water-impermeable multilayer article |
| JP6804149B2 (ja) * | 2016-12-05 | 2020-12-23 | 花王株式会社 | フィルム状触媒の保護材巻取装置および方法 |
| WO2018111731A1 (en) * | 2016-12-15 | 2018-06-21 | Angela Johnson | A cosmetic applicator and method |
| CN110091549B (zh) * | 2019-05-15 | 2020-10-20 | 东莞顺裕纸业有限公司 | 一种瓦楞纸板芯纸加工装置 |
| CN110180963B (zh) * | 2019-05-30 | 2025-01-03 | 兰州兰石能源装备工程研究院有限公司 | 一种薄板成型压机自动上下料装置 |
| CN113976700A (zh) * | 2021-10-25 | 2022-01-28 | 淄博气宇空调节能设备有限公司 | 金属瓦楞的制作方法 |
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- 2009-04-03 EP EP09727047.4A patent/EP2260941B1/en not_active Not-in-force
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Also Published As
| Publication number | Publication date |
|---|---|
| EP2260941B1 (en) | 2016-09-14 |
| JP5449823B2 (ja) | 2014-03-19 |
| CN101990465B (zh) | 2012-10-31 |
| US20110065569A1 (en) | 2011-03-17 |
| EP2260941A4 (en) | 2012-10-03 |
| US8501665B2 (en) | 2013-08-06 |
| EP2260941A1 (en) | 2010-12-15 |
| CN101990465A (zh) | 2011-03-23 |
| JP2009262145A (ja) | 2009-11-12 |
| ES2605238T3 (es) | 2017-03-13 |
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