JP5436011B2 - Water-in-oil emulsion for foam sheet and method for preparing the same, and foam sheet and method for producing the same - Google Patents

Description

  The present invention relates to a novel water-in-oil emulsion containing no emulsifier and a method for preparing the same. The present invention further relates to a method for producing a foam sheet using such a water-in-oil emulsion and the foam sheet obtained thereby. The resulting foam may be closed or open, depending on the microstructure of the water-in-oil emulsion.

  Water-in-oil emulsions with a relatively high water relative oil phase ratio are known in the art as High Internal Phase Emulsion ("HIPEs" or "HIPE" emulsions).

  The properties and properties of the porous polymer foam material formed by polymerizing the HIPE emulsion also vary greatly depending on the type of components that make up the polymerizable HIPE emulsion and the conditions of each process used to form the emulsion. It is known. For example, a method for preparing an absorbent porous polymer (ie, foam) from a highly discontinuous phase emulsion comprising at least 90% by weight of water and an oil phase comprising a polymerizable monomer and a surfactant and a polymerization catalyst (patent) Reference 1), or a high discontinuous phase emulsion comprising at least an aqueous phase, a polymerizable monomer, and a surfactant and a polymerization catalyst. A method of preparing a dry hydrophobic foam having a dry density of less than and a toughness index of at least about 75 (Patent Document 2) has been proposed. A method for producing a porous cross-linked polymer capable of continuously performing from the supply of HIPE to the polymerization is also disclosed (Patent Document 3). Furthermore, a method for producing a foam by photopolymerizing HIPE is disclosed (Patent Document 4).

  Although the existence and synthesis of polymerizable HIPE emulsions are known in the art, as described in the above patent document, there is no problem in preparing HIPE emulsions suitable for polymerizing them into useful foam materials. Is not something that is done. Such a HIPE emulsion, specifically, a HIPE emulsion having a very high water relative oil phase ratio, tends to be unstable. Even if the monomer / crosslinker content that is the continuous phase component of water-in-oil emulsions, the choice of emulsifier type, the concentration and temperature of the emulsion components, and / or the stirring conditions change only slightly, these emulsions are “broken”. They may clearly separate at least some into the water and oil phases. In particular, in order to obtain an emulsion that is stable to emulsification, the incorporation of an emulsifier is essential, and sorbitan monooleate, inorganic fine particles subjected to surface hydrophobization treatment and layered clay mineral are used as a lipophilic emulsifier. Alternatively, a method for preparing a water-in-oil emulsion containing fine solid spherical particles of polyalkylsilesquioxane without containing a surfactant is disclosed (Patent Document 5).

  Therefore, an emulsifier or an emulsifier substitute material is essential for the formation of stable HIPE. Typically, an emulsifier or the like is added to 100 parts by weight of the reactive phase in the continuous oil phase composed of the reactive phase and the emulsifier. It is necessary to constitute up to 30 parts by weight. For this reason, even if a stable emulsion is obtained, if the emulsion composition and processing conditions change, the properties and characteristics of the final polymeric foam material may be significantly affected. May be significantly different from the desired physical properties.

  In contrast, reactive emulsifiers have also been studied to introduce emulsifiers and alternative materials that may act as contaminants in the foams that form into the continuous phase that makes up the polymer foam material. For example, a method for preparing a foam from a water-in-oil emulsion containing functionalized metal oxide nanoparticles as an emulsifier substitute material is disclosed (Patent Document 6).

  However, such conventional water-in-oil emulsions, especially HIPE emulsions, tend to be unstable. In particular, when obtaining foam materials from such emulsions, the emulsions formed should be prepared to produce a polymerizable emulsion by a continuous process to provide the foam material in a commercially useful or required amount for development. The stability of the foam material is not sufficient, and the physical properties of the foam material may be significantly different from the intended physical properties due to the influence of the emulsifier substitute material.

  Further, most of the foams formed from water-in-oil type HIPE emulsions generally containing an emulsifier have an open cell structure in which a large number of openings are present in the cell walls. There is no disclosure of a method for selectively forming both closed and open cell structures in the presence of alternative materials.

Japanese Examined Patent Publication No. 3-66323 Special table 2003-514052 gazette Special table 2001-163904 gazette Japanese translation of PCT publication No. 2003-510390 Japanese Patent No. 2656226 JP-T-2004-504461

  An object of the present invention is to provide a water-in-oil emulsion containing a HIPE emulsion that is substantially free of an emulsifier and is excellent in stability for polymerization into a foam sheet, and a method for preparing the same.

  Another object of the present invention is to provide a method for producing a foam sheet from such a water-in-oil emulsion and a foam sheet obtained thereby.

  As a result of intensive studies to solve the above problems, the present inventors have found the following water-in-oil emulsion and have completed the present invention.

That is, the present invention contains the following components (a) and (b), and does not contain an emulsifier:
(A) i) a polymerizable monomer composition comprising an ethylenically unsaturated monomer and at least one polar monomer copolymerizable with the ethylenically unsaturated monomer, ii) an ethylenically unsaturated monomer and the ethylenically unsaturated monomer A weight average molecular weight of at least one polymer obtained by polymerizing at least one polar monomer copolymerizable with a saturated monomer and having a weight average molecular weight of 100,000 to 10,000,000, and 5% by weight with respect to the total amount of i) % Of a polymer, iii) a continuous oil phase component comprising at least one polymerization initiator, and iv) at least one crosslinking agent; and (b) at least one immiscible with the continuous oil phase component Co-continuous or discontinuous phase components,
About.

The ethylenically unsaturated monomer of i) and the ethylenically unsaturated monomer of ii) are both at least one alkyl (meth) acrylate having 1 to 20 carbon atoms in the alkyl group, and in i) The ratio of at least one alkyl (meth) acrylate having 1 to 20 carbon atoms in the alkyl group to at least one polar monomer copolymerizable with the alkyl (meth) acrylate is 70 to 98 parts by weight 2 to 30 parts by weight,
The ratio of at least one alkyl (meth) acrylate having 1 to 20 carbon atoms in the alkyl group in ii) to at least one polar monomer copolymerizable with the alkyl (meth) acrylate is 70 to 95. It is preferably 5 to 30 parts by weight.

  The water-in-oil emulsion comprises at least one alkyl (meth) acrylate having 1 to 20 carbon atoms in the alkyl group and at least one polar monomer copolymerizable with the alkyl (meth) acrylate, After partial polymerization of a polymerizable composition comprising 70 to 95 parts by weight to 5 to 30 parts by weight, the proportion of unpolymerized monomer is adjusted to 70 to 98 parts by weight to 2 to 30 parts by weight. Can be.

  The weight average molecular weight of the ii) polymer is preferably 100,000 or more and 500,000 or less.

  The ii) polymer is preferably 20% by weight or more based on the total amount with the above i).

  The amount of the crosslinking agent in the continuous oil phase component is preferably 5 to 30 parts by weight with respect to 100 parts by weight of the mixed syrup of i) and ii).

  The co-continuous or discontinuous phase component is preferably water.

  It is preferred that the co-continuous or discontinuous phase component comprises at least 74 volume percent of the total emulsion.

The present invention is also a method for preparing a water-in-oil emulsion,
(a) i) at least one alkyl (meth) acrylate having 1 to 20 carbon atoms in the alkyl group and at least one polar monomer copolymerizable with the alkyl (meth) acrylate, 70 to 95 weight A step of partially polymerizing a polymerizable composition comprising 5 to 30 parts by weight and then adjusting the proportion of unpolymerized monomer to 70 to 98 parts by weight to 2 to 30 parts by weight to obtain a prepolymer syrup;
iii) obtaining a continuous oil phase component by mixing at least one polymerization initiator and at least one crosslinking agent in the prepolymer syrup;
(b) mixing the continuous oil phase component with the immiscible at least one co-continuous or discontinuous phase component without adding an emulsifier;
A preparation method comprising:

The present invention also includes (a) preparing and shaping any of the above water-in-oil emulsions;
(b) exposing the water-in-oil emulsion to thermal energy, far-infrared rays, ultraviolet rays, or visible light capable of activating the polymerization initiator in the water-in-oil emulsion to form a water-containing crosslinked polymer; And (c) a step of dehydrating the water-containing crosslinked polymer, and a method for producing a foam sheet.

  In the method for producing a foam sheet, (a) a preparation and molding step of the water-in-oil emulsion, (b) a formation step of the water-containing crosslinked polymer, and (c) a dehydration step of the water-containing crosslinked polymer are continuous. It is preferable to be carried out automatically.

  The present invention also relates to a foam sheet obtained from the above-mentioned water-in-oil emulsion and having an open cell structure and / or an open cell structure having openings between the cells.

  The present invention also relates to a foam sheet obtained from the water-in-oil emulsion and having an open cell structure having an average cell diameter of 20 μm or less and an opening between the cells.

  Even if it does not contain an emulsifier, the water-in-oil emulsion of the present invention is excellent in stability and can be polymerized into a foam sheet. Such water-in-oil emulsions enable the stable production of foam sheets on a continuous and commercially available scale.

  According to the present invention, it is possible to selectively form a closed cell structure or an open cell structure in the production of a foam sheet.

  Furthermore, in the conventional foam molding method, it is necessary to prepare the foam thickness by processing such as slicing. However, in the foam sheet of the present invention, the monomer composition is formed into a sheet shape with an arbitrary thickness. It is possible to produce a foam sheet having a desired thickness continuously with high accuracy.

  The foam sheet of the present invention has a three-dimensional network structure by crosslinking, and has excellent heat resistance and compression recovery.

1 shows a cross-sectional SEM photograph (800 times) of an acrylic resin foam obtained in Example 1. FIG. A cross-sectional SEM photograph (1200 times) of the acrylic resin foam obtained in Example 2 is shown. 2 is a cross-sectional SEM photograph (1,200 times) of the acrylic resin foam obtained in Example 3. A cross-sectional SEM photograph (1,200 times) of the acrylic resin foam obtained in Example 4 is shown. A cross-sectional SEM photograph (1,200 times) of the acrylic resin foam obtained in Example 5 is shown. A cross-sectional SEM photograph (800 times) of the acrylic resin foam obtained in Example 6 is shown. 2 shows a cross-sectional SEM photograph (800 times) of the acrylic resin foam obtained in Example 7. FIG. A cross-sectional SEM photograph (800 times) of the acrylic resin foam obtained in Example 8 is shown. A cross-sectional SEM photograph (800 times) of the acrylic resin foam obtained in Example 9 is shown. 2 is a cross-sectional SEM photograph (800 times) of the acrylic resin foam obtained in Example 10. FIG. A cross-sectional SEM photograph (800 times) of the acrylic resin foam obtained in Comparative Example 2 is shown. A cross-sectional SEM photograph (800 times) of the acrylic resin foam obtained in Comparative Example 3 is shown.

  The water-in-oil emulsion of the present invention contains the following components and does not contain an emulsifier.

  (A) i) a polymerizable monomer composition comprising an ethylenically unsaturated monomer and at least one polar monomer copolymerizable with the ethylenically unsaturated monomer, ii) an ethylenically unsaturated monomer and the ethylene And at least one polymer having a weight average molecular weight of 100,000 to 10,000,000 obtained by polymerizing at least one polar monomer copolymerizable with the polymerizable unsaturated monomer, with respect to the total amount of said i) 5% by weight or more of a polymer, iii) a continuous oil phase component comprising at least one polymerization initiator, and iv) at least one crosslinking agent; and (b) at least one immiscible with the continuous oil phase component Contains species co-continuous or discontinuous phase components.

  Here, the ethylenically unsaturated monomer in i) and ii) is not limited, but is preferably at least one alkyl (meth) acrylate having 1 to 20 carbon atoms in the alkyl group.

  In this specification, the term “alkyl (meth) acrylate having 1 to 20 carbon atoms in an alkyl group” refers to a linear or branched alkyl group having 1 to 20 carbon atoms (meta ) Refers to acrylates and excludes those containing an aromatic ring in the structure. The average carbon number of the alkyl group is preferably 2-18. (Meth) acrylate refers to acrylate and / or methacrylate, and (meth) of the present invention has the same meaning.

  Specific examples of the alkyl (meth) acrylate include, for example, methyl group, ethyl group, propyl group, butyl group, amyl group, hexyl group, heptyl group, 2-ethylhexyl group, isooctyl group, isononyl group, isodecyl group, dodecyl group, A linear or branched alkyl group having 1 to 20, preferably 4 to 18 carbon atoms, such as lauryl group, tridecyl group, tetradecyl group, pentadecyl group, hexadecyl group, heptadecyl group, octadecyl group, nonadecyl group, and eicosyl group And those using one or more of esters of acrylic acid and methacrylic acid having the above. More specifically, methyl (meth) acrylate, ethyl (meth) acrylate, propyl (meth) acrylate, n-butyl (meth) acrylate, s-butyl (meth) acrylate, t-butyl (meth) acrylate, isobutyl ( (Meth) acrylate, n-pentyl (meth) acrylate, isopentyl (meth) acrylate, hexyl (meth) acrylate, heptyl (meth) acrylate, isoamyl (meth) acrylate, 2-ethylhexyl (meth) acrylate, n-octyl (meth) ) Acrylate, isooctyl (meth) acrylate, n-nonyl (meth) acrylate, isononyl (meth) acrylate, n-decyl (meth) acrylate, isodecyl (meth) acrylate, n-dodecyl (meth) acrylate, isomi Still (meth) acrylate, n-tridecyl (meth) acrylate, n-tetradecyl (meth) acrylate, stearyl (meth) acrylate, lauryl (meth) acrylate, pentadecyl (meth) acrylate, hexadecyl (meth) acrylate, heptadecyl (meth) Examples include acrylate, octadecyl (meth) acrylate, nonadecyl (meth) acrylate, eicosyl (meth) acrylate, and isostearyl (meth) acrylate. Especially, n-butyl (meth) acrylate, 2-ethylhexyl (meth) acrylate, etc. can be illustrated and these can be used individually or in combination of 2 or more types. Alkyl (meth) acrylates may be used in combination of two or more, and in the same emulsion, the alkyl (meth) acrylates of i) and ii) may be the same, part of them may be the same or different. Also good.

  In the present invention, the “polar monomer” includes (meth) acrylic acid, carboxyethyl (meth) acrylate, carboxypentyl (meth) acrylate, ω-carboxy-polycaprolactone monoacrylate, monohydroxyethyl acrylate phthalate, itaconic acid, malee Carboxyl group-containing monomers such as acid, fumaric acid and crotonic acid; acid anhydride monomers such as maleic anhydride and itaconic anhydride; 2-hydroxyethyl (meth) acrylate, 2-hydroxypropyl (meth) acrylate, (meta ) 4-hydroxybutyl acrylate, 6-hydroxyhexyl (meth) acrylate, 8-hydroxyoctyl (meth) acrylate, 10-hydroxydecyl (meth) acrylate, 12-hydroxylauryl (meth) acrylate, (4 -Hydroxyme Hydroxyl group-containing monomers such as tilcyclohexyl) methyl (meth) acrylate; amide group-containing monomers such as N, N-dimethyl (meth) acrylamide and N, N-diethyl (meth) acrylamide, and the like. It can be used in combination of more than one species.

  The weight ratio of the ethylenically unsaturated monomer contained in the polymerizable monomer composition i) and the polar monomer copolymerizable therewith is preferably 70 to 98 parts by weight to 2 to 30 parts by weight. This weight is more preferably 75 to 96 parts by weight to 4 to 25 parts by weight, and still more preferably 80 to 95 parts by weight to 5 to 20 parts by weight. If the amount of the polar monomer used is in the range of 2 parts by weight or more and 30 parts by weight or less, ii) the solubility of the polymer is maintained and a more stable water-in-oil emulsion is formed.

  The component of the alkyl (meth) acrylate having 1 to 20 carbon atoms in the alkyl group contained in the polymer of ii) and the polar monomer copolymerizable therewith is 70 to 95 parts by weight to 5 to 30 by weight. It is preferable that it is a weight part. This weight is more preferably 80 to 95 parts by weight to 5 to 20 parts by weight, and still more preferably 85 to 94 parts by weight to 6 to 15 parts by weight. If the amount of the polar monomer constituting the polymer is in the range of 5 to 30 parts by weight, the ratio of the co-continuous or discontinuous phase component to the continuous oil phase does not decrease, and good in the emulsification process This is preferable because it is maintained.

  In addition, the molecular weight and concentration of the polymer are mainly determined in the formation of a water-in-oil emulsion, such as the continuous oil phase component a) constituting the water-in-oil emulsion, the liquid properties of the water-in-oil emulsion, the surface activity, It is thought that it affects the film strength of the droplets, the storage stability at rest, and the cell structure of the resulting foam sheet. In particular, the molecular weight of the polymer ii) and its concentration are very closely related to the coating strength and size of the water droplets in the water-in-oil emulsion, and it is expected that the water droplet size will decrease as the concentration of the polymer iii) increases. And the bubble diameter of the obtained foam sheet also becomes small. Further, since the coating strength of water droplets is expected to be reduced due to the decrease in molecular weight and an opening is formed in the bubble wall, the desired bubble diameter and bubble structure can be selected by appropriately selecting the molecular weight and concentration of the polymer ii). A water-in-oil emulsion and a foam sheet are obtained. The concentration of polymer ii) is sufficient to obtain a water-in-oil emulsion with fine water droplets and a surface active action sufficient to mold a foam having a cell diameter, and a polymerization of i). 5% by weight or more based on the total amount of the polymerizable monomer composition and the polymer. Preferably, it is 7% by weight or more, more preferably 10% by weight or more, and most preferably 20% by weight or more. The upper limit is not particularly limited, but is preferably 50% by weight or less, more preferably 40% by weight or less, and still more preferably 30% by weight or less.

  In the present specification, a mixture of i) a polymerizable monomer composition and ii) a polymer may be referred to as a prepolymer syrup or a mixed syrup.

  Here, about 0.5 g of the mixed syrup of i) and ii) is precisely weighed, and the weight after drying this at 130 ° C. for 2 hours is precisely weighed to reduce the weight loss (volatile matter (unreacted)). The monomer weight)) can be determined and calculated by the following equation.

  % By weight of polymer in mixed syrup = [1- (weight loss) / (weight of mixed syrup before drying)] × 100

  Further, the molecular weight of the polymer ii) is sufficient to obtain a surface active action and film strength sufficient to form a water-in-oil emulsion having stable storage stability and a foam capable of selecting any cell structure. Therefore, the weight average molecular weight is 100,000 to 10,000,000, preferably 100,000 to 7,000,000, more preferably 100,000 to 6.5 million, and most preferably 100,000 to 500,000.

The weight average molecular weight (Mw) can be measured by gel permeation chromatograph (GPC). More specifically, as a GPC measurement device, the product name “HLC-8020GPC” (manufactured by Tosoh Corporation) can be used to measure and obtain the value in terms of polystyrene under the following GPC measurement conditions.
GPC measurement conditions and sample concentration: 0.1% by weight (tetrahydrofuran solution)
Sample injection volume: 100 μl
・ Eluent: Tetrahydrofuran (THF)
・ Flow rate (flow rate): 0.5 mL / min
Column temperature (measurement temperature): 40 ° C
Column: Trade name “TSKgel GMH _HR- H (20)” (manufactured by Tosoh Corporation)
・ Detector: Differential refractometer

  The prepolymer syrup that is a mixture of i) and ii) can be obtained by partial polymerization of a composition having the same composition as the polymerizable monomer composition of i), although not limited thereto.

  The method for producing a prepolymer syrup by partially polymerizing the polymerizable composition is not particularly limited, and a known polymer syrup production method can be applied. Such a method is not limited. For example, the polymerizable composition contains a small amount of a polymerization initiator, and is exposed to thermal energy, ultraviolet rays, far infrared rays, visible light, or the like depending on the kind of the polymerization initiator. And adjusting to the desired viscosity and base. The viscosity of the prepolymer syrup is not limited, but is preferably 1 to 50 Pa · s, more preferably 5 to 30 Pa · s, and still more preferably 5 to 20 Pa · s. Here, the viscosity is measured at 25 ° C. using a B-type viscosity type.

  The prepolymer syrup that is a mixture of i) and ii) is also polymerized by charging a polymerizable monomer composition having the same composition as i) with a chain transfer agent, a polymerization initiator, etc. in an arbitrary solvent. Any method for synthesizing a polymer that satisfies the above conditions, such as a solution polymerization method in which a soluble monomer composition, a chain transfer agent, and a polymerization initiator are dissolved, and the resulting polymer is washed with a poor solvent that does not dissolve Can be produced.

  In particular, it is desirable to use a partial polymerization method when the weight average molecular weight of the polymer is 500,000 or more, and a solution polymerization method when the weight average molecular weight is less than 500,000.

  In the partial polymerization method, the composition of the polymerizable monomer composition after polymerization is the same as the composition constituting the polymer obtained by partial polymerization, or the polymer ii) is compatible with the polymer i). If it is a composition, adjusting the kind and combination of the said ethylenically unsaturated monomer and polar monomer on the conditions which satisfy | fill the range of 2-30 weight part of polar monomers with respect to 70-98 weight part of said ethylenically unsaturated monomers. Is possible.

  In the present invention, the polymerization initiator used in achieving the partial polymerization in the above-mentioned prepolymer syrup, or mixed with the prepolymer syrup and used to prepare the continuous oil phase component of the present invention iii) The polymerization initiator as a component includes a polymerization initiator such as a radical polymerization initiator, an anionic polymerization initiator, and a cationic polymerization initiator. Furthermore, examples of the radical polymerization initiator include a thermal polymerization initiator, a photopolymerization initiator, and a redox polymerization initiator. Examples of the thermal polymerization initiator include azo compounds, peroxides, peroxycarbonic acid, peroxycarboxylic acid, potassium persulfate, t-butylperoxyisobutyrate, and 2,2′-azobisisobutyronitrile. . Examples of the photopolymerization initiator include 4- (2-hydroxyethoxy) phenyl (2-hydroxy-2-propyl) ketone (for example, Ciba Japan, trade name: Darocur 2959), α-hydroxy-α, α '-Dimethylacetophenone (for example, Ciba Japan, trade name: Darocur 1173), methoxyacetophenone, 2,2-dimethoxy-2-phenylacetophenone (for example, Ciba Japan, trade name: Irgacure 651), Acetophenone photopolymerization initiators such as 2-hydroxy-2-cyclohexylacetophenone (for example, Ciba Japan, trade name: Irgacure 184), ketal photopolymerization initiators such as benzyldimethyl ketal, and other halogenated ketones , Acylphosphine oxide (for example, Ciba Japan, trade name; Rugakyua 819), and the like. These polymerization initiators may be used alone or in combination of two or more.

  In the case of the polymerization initiator used for achieving the partial polymerization in the prepolymer syrup, the amount of the polymerization initiator used is 0.1% with respect to 100 parts by weight of the mixed monomer of alkyl (meth) acrylate and polar monomer. It is 03-1 weight part, Preferably, it is 0.05-0.5 weight part.

  The amount of the polymerization initiator mixed with the prepolymer syrup is, depending on the combination of the monomer component and the polymerization initiator, a prepolymer syrup or a continuous oil phase component composed of the prepolymer syrup and a crosslinking agent. It is preferable that it is the range of 0.05-5.0 weight part with respect to 100 weight part of the whole, More preferably, it is 0.1-1.0 weight part. When the amount of the polymerization initiator used is less than 0.05 parts by weight, the amount of unreacted monomer components may increase, and the amount of residual monomers in the resulting porous material tends to increase. become. On the other hand, when the usage-amount of the said polymerization initiator exceeds 5.0 weight part, the mechanical property of the foam material obtained may deteriorate.

  Note that the amount of radicals generated by the photopolymerization initiator varies depending on the type and intensity of light to be irradiated, time, the amount of dissolved oxygen in the monomer and solvent mixture, and the like. When the amount of dissolved oxygen is large, the amount of radicals generated is suppressed, the polymerization does not proceed sufficiently, and unreacted substances may increase. Therefore, before the light irradiation, it is preferable that an inert gas such as nitrogen is blown into the composition to replace oxygen with nitrogen.

  When a photopolymerization initiator is used as the polymerization initiator, it can be produced without containing an environmentally hazardous substance such as an organic solvent, if desired. Furthermore, it is not necessary to heat the monomer composition during polymerization. Therefore, it is not necessary to consider the foaming temperature of the foaming agent to be added, and it is possible to use a low-temperature foaming type foaming agent. When a photopolymerization initiator is used, a foam sheet having a desired molecular structure can be reliably obtained during the photopolymerization process.

  The cross-linking agent used in the present invention is typically present to connect polymer chains together to produce a more three-dimensional molecular structure. The selection of the particular type and amount of crosslinker depends on the structural, mechanical, and fluid treatment characteristics desired for the resulting foam. The selection of the specific type and amount of crosslinker is important in the final realization of the preferred foam with the desired combination of structure and mechanical properties. Such cross-linking agents include methacrylates, acrylamides, methacrylamides and mixtures thereof. These include di, tri and tetra-acrylates, di, tri and tetra-methacrylates, di, tri and tetra-acrylamides, di, tri and tetra-methacrylamides, and mixtures of these crosslinkers. Suitable acrylate and methacrylate crosslinkers can be derived from diols, triols and tetraols including 1,10 decanediol, 1,8 octanediol, 1,6 hexanediol, 1,4 butanediol, 1, 3 butanediol, 1,4 butane 2ene diol, ethylene glycol, diethylene glycol, trimethylolpropane, pentaerythritol, hydroquinone, catechol, resorcinol, triethylene glycol, polyethylene glycol, sorbitol, etc. (acrylamide and methacrylamide crosslinkers are Can be derived from the corresponding diamines, triamines and tetraamines). Preferred diols have at least 2, more preferably at least 4, and most preferably 6 carbon atoms. The amount of the crosslinking agent used depends on the combination of the alkyl (meth) acrylate and the polar monomer constituting the continuous oil phase component, but is at least one prepolymer syrup obtained by partially polymerizing the polymerizable composition. It is preferable that it is the range of 5-30 weight part with respect to a part, More preferably, it is 10-30 weight part. When the amount of the crosslinking agent used is less than 5 parts by weight, the cell structure may collapse due to shrinkage in the step of dehydrating the water-containing crosslinked polymer as the heat resistance decreases. On the other hand, when the usage-amount of the said crosslinking agent exceeds 30 weight part, the mechanical property of the foam material obtained may deteriorate.

  The continuous oil phase component of the present invention is thus a polymerizable monomer composition comprising (a) i) an ethylenically unsaturated monomer and at least one polar monomer copolymerizable with the ethylenically unsaturated monomer, ii) at least one polymer having a weight average molecular weight of 100,000 to 10,000,000 obtained by polymerizing an ethylenically unsaturated monomer and at least one polar monomer copolymerizable with the ethylenically unsaturated monomer, It can be obtained by uniformly mixing a polymer that is 5% by weight or more with respect to the total amount with i), iii) at least one polymerization initiator, and iv) at least one crosslinking agent.

  The co-continuous or discontinuous phase component b) used in the present invention can use any fluid that is substantially immiscible with the continuous oil phase component. The best known immiscible fluid is water. The immiscible fluid may contain a photopolymerization initiator.

  The water-in-oil emulsion of the present invention does not require a salt or the like to stabilize the emulsion, but a salt or a water-soluble polymer compound may be added. Examples of the salt include, but are not limited to, sodium carbonate, calcium carbonate, potassium carbonate, sodium phosphate, calcium phosphate, potassium phosphate, sodium chloride, potassium chloride and the like. Examples of the water-soluble polymer compound include polyvinyl alcohol (PVA), polyacrylic acid and derivatives thereof, synthetic polymer compounds such as polyethylene oxide and polyvinyl pyrrolidone, and cellulose ethers such as hydroxypropylmethylcellulose and hydroxyethylcellulose. . Among these, in particular, PVA having a saponification degree of 97 mol% or more and a polymerization degree of 1000 or more can be preferably used.

  The relative amount of the co-continuous or discontinuous phase component that is immiscible with the continuous oil phase component used to form the water-in-oil emulsion of the present invention depends on the structural, mechanical, and performance of the resulting polymer foam. Is important in determining physical characteristics. Because the volume ratio of the continuous oil phase component to the immiscible co-continuous or discontinuous phase component affects the characteristics of the foam, such as density, cell size, cell structure, and the dimensions of the walls that form the foam structure. When it is desired to obtain a rigid foam foam, the discontinuous phase component is decreased. When a flexible foam foam is desired, the discontinuous phase component is increased.

  Specifically, in the present invention, the entire emulsion is kept stable even in a state where the proportion of immiscible co-continuous or discontinuous phase components is high. For this reason, the immiscible co-continuous or discontinuous phase component may be 74% by volume or more, and preferably 74% by volume or more and 99% by volume or less, based on the whole emulsion.

  The density and microstructure of the foam will also depend on the mode of production of the emulsion, that is, the rate of addition of the immiscible co-continuous or discontinuous phase component to the continuous oil phase component, the stirring method. Therefore, when obtaining a fine structure, it is preferable to slow down the addition rate and add under high shear conditions. When increasing the diameter, it is preferred to speed up the addition and add under low shear conditions.

  Emulsions are typically prepared by methods such as shaking using an emulsifier such as a blade mixer or pin mixer, and use of a magnetic stir bar under low shear conditions, i.e., providing gentle mixing of the continuous and dispersed phases. Is done.

  High shear conditions may be achieved by a rotor-stator mixer, a homogenizer, or a microfluidizer. The emulsion of the present invention may be produced by continuous or batch operation.

  Suitable equipment for continuously producing the emulsion includes a static mixer, a rotor-stator mixer, and a pin mixer. More intense agitation may be achieved by increasing the agitation speed or by using an apparatus designed to finely disperse the emulsifier in the emulsion by a mixing method. Batch process emulsions may be made by mixing or shaking the combined ingredients by hand or machine. For example, a driven blade mixer or a three-blade propeller mixing blade may be used to achieve more intense agitation in the batch process.

  In addition, the water-in-oil emulsion contains, as optional components, tackifying resin, talc, calcium carbonate, magnesium carbonate, silicic acid and its salts, clay, mica powder, aluminum hydroxide, magnesium hydroxide, zinc white, vent Nine, carbon black, silica, alumina, aluminum silicate, acetylene black, aluminum powder and other conventionally known additives such as pigments and dyes are used as long as they do not impair emulsion stability and polymerization reactivity. Can be blended.

  In the present invention, in order to shape and polymerize a water-in-oil emulsion, in the formation of a water-in-oil emulsion, a continuous oil phase component and a co-continuous or discontinuous phase component are continuously supplied to an emulsifier. Form a water-in-water emulsion, polymerize the resulting water-in-oil emulsion to obtain a water-containing cross-linked polymer, followed by a “continuous method” in which the water-containing cross-linked polymer is continuously dehydrated, The aqueous phase and the oil phase in an amount can be supplied to an emulsifier, and a water-containing cross-linked polymer can be obtained using a water-in-oil emulsion in the emulsifier, and then dehydrated. The continuous polymerization method in which the water-in-oil emulsion is continuously polymerized is a preferable method because the production efficiency is high and the effect of shortening the polymerization time and the shortening of the polymerization apparatus can be most effectively utilized.

  Specifically, as a continuous polymerization method for a sheet-like porous polymer, a water-in-oil emulsion of the present invention is continuously applied on a traveling belt having a structure in which the belt surface of a belt conveyor is heated by a heating device. A method of polymerizing by heating while forming a smooth sheet on the belt; or using a device that irradiates actinic radiation in place of the heating device, and on the running belt of the present invention. There is a method in which a water-in-oil emulsion is continuously fed and polymerized by actinic light while forming a smooth sheet on a belt.

  Therefore, as one aspect, a porous polymer can be obtained by supplying a water-in-oil emulsion to the polymerization apparatus and heating it. In the water-in-oil emulsion of the present invention, it is preferable to heat the water-in-oil emulsion in the range of from room temperature to 150 ° C., more preferably from 60 to 150 from the viewpoint of the stability of the water-in-oil emulsion and the polymerization rate. The range of ° C., more preferably 70 to 130 ° C., and particularly preferably 80 to 100 ° C. When the polymerization temperature is less than room temperature, the polymerization takes a long time, which is not preferable for industrial production. On the other hand, when the polymerization temperature exceeds 150 ° C., the pore diameter of the obtained porous material becomes non-uniform, and the strength of the porous material is lowered, which may be undesirable. Further, the polymerization temperature may be changed in two stages or even multiple stages during the polymerization, and this polymerization method is not excluded.

  On the other hand, in consideration of productivity, a method of polymerizing and crosslinking by forming water-in-oil emulsions and then exposing them to actinic rays such as ultraviolet rays and visible rays is also preferably used.

  At this time, after the water-in-oil emulsions are formed, they may be exposed to actinic radiation such as ultraviolet rays and visible rays to be polymerized and crosslinked. Preferably, light in the visible and / or ultraviolet range (200 nm to 800 nm) is used to polymerize the water-in-oil emulsion of the present invention. Since water-in-oil emulsions have a strong tendency to scatter light, it is preferable to use long wavelengths in this range that can better penetrate water-in-oil emulsions. Preferred wavelengths are 200-800 nm, more preferably 300-800 nm, most preferably 300-450 nm due to the availability of photoinitiators that can be activated at these wavelengths and the availability of light sources. . The photopolymerization initiator used must be able to absorb the wavelength (s) of the light source used. In the present invention, as a typical lamp used for light irradiation, an ultraviolet lamp capable of performing ultraviolet irradiation includes a lamp having a spectral distribution in a wavelength region of 300 to 400 nm. Examples thereof include a chemical lamp and a black light. (Trade name manufactured by Toshiba Lighting & Technology Co., Ltd.), metal halide lamps.

  The ultraviolet illuminance in the present invention is set to the desired illuminance by adjusting the distance from the ultraviolet lamp to the ultraviolet irradiated object (water-in-oil emulsion) and the voltage, but this is disclosed in JP-A-2003-13015. In the method, ultraviolet irradiation in each step is performed in a plurality of stages, whereby the adhesion performance can be adjusted more precisely. This ultraviolet irradiation is carried out in a nitrogen gas atmosphere, an inert gas atmosphere, or flowed to the substrate in order to prevent the influence of oxygen having a polymerization inhibiting action on the polymer polymerization rate, the molecular weight and the molecular weight distribution from being obtained as much as possible. It is preferable to carry out by laminating a film which blocks ultraviolet rays such as polyethylene terephthalate coated with a release agent such as silicone, but blocks oxygen, on the spread ultraviolet ray polymerizable monomer composition.

  In the method for producing a foam sheet according to the present invention, for example, the water-in-oil emulsion is coated on one surface of a thermoplastic resin film, and is coated with a release agent such as silicone under an inert gas atmosphere. A step of irradiating light in a state where oxygen is blocked by coating with a film can also be included.

  Examples of such a thermoplastic resin film include, but are not limited to, plastic films and sheets such as polyester, olefin resin, and polyvinyl chloride.

  In the present invention, the method for coating the water-in-oil emulsion on one surface of the substrate is not particularly limited, and it is performed using a commonly used roll coater, die coater, knife coater, or the like. Can do.

  In the present invention, the inert gas atmosphere during photopolymerization refers to an atmosphere in which oxygen in the light irradiation zone is replaced with an inert gas such as nitrogen. Accordingly, it is desirable that oxygen is not present as much as possible in the inert gas atmosphere, and the oxygen concentration is preferably 5000 ppm or less.

  After polymerizing the water-in-oil emulsion, the co-continuous or discontinuous phase components are typically still present in the porous polymer. This residual co-continuous or discontinuous phase component may be removed by drying the porous polymer. Suitable drying methods include, for example, vacuum drying, freeze drying, press drying, microwave drying, drying in a heat oven, infrared drying, or a combination of these techniques.

  Many polymer foams made from the above water-in-oil emulsions of the present invention are typically closed cell, but open cell foams can also be made. This means that most or all of the bubbles are in undisturbed communication with adjacent bubbles.

  Foam bubbles, particularly those formed by polymerization of a monomer-containing continuous oil phase surrounding a relatively monomer-free, immiscible, co-continuous or discontinuous phase droplet, tend to be substantially spherical in shape. For most applications, the bubble size is typically in the range of 1 to 200 μm, preferably 100 μm or less, more preferably 50 μm or less, and most preferably 20 μm or less.

  The foam sheet of the present invention is suitable for countless applications including cushion materials, insulation, heat insulating materials, soundproof materials, dustproof materials, filter materials, and the like.

  EXAMPLES The present invention will be specifically described below with reference to examples, but the present invention is not limited to these examples. In addition, the part in each example is based on weight, and% is based on capacity. Evaluation items in Examples and the like were measured as follows.

(Preparation of mixed syrup by partial polymerization method)
90 parts by weight of 2-ethylhexyl acrylate (made by Toa Gosei Co., Ltd., hereinafter abbreviated as “2EHA”) as an ethylenically unsaturated monomer, and acrylic acid (from Toa Gosei Co., Ltd., hereinafter abbreviated as “AA”) as a polar monomer ) 0.05 parts by weight of 2,2-dimethoxy-1,2-diphenylethane-1-one (trade name “Irgacure 651” manufactured by Ciba Japan Co., Ltd.) per 100 parts by weight of the mixed monomer solution consisting of 10 parts by weight , 1-hydroxy-cyclohexyl-phenyl-ketone (trade name “Irgacure 184”, manufactured by Ciba Japan Co., Ltd.) was added to a four-necked flask, and the solution was added under a nitrogen atmosphere and a room temperature atmosphere. A partially polymerized syrup 1 having a polymer concentration of 7.2% was obtained by partial photopolymerization by exposure to ultraviolet light. The weight average molecular weight of the produced polymer was 6 million.

(Preparation of mixed syrup 2 by partial polymerization method)
In the preparation of mixed syrup 1, mixed syrup 2 having a partially polymerized polymer concentration of 25.0% was obtained by the same operation as the preparation of mixed syrup 1, except that the polymerization start temperature was 80 ° C. The weight average molecular weight of the produced polymer was 1,070,000.

(Preparation of mixed syrup 3 by partial polymerization method)
In preparation of the mixed syrup 2, a mixed monomer solution consisting of 2EHA having the same composition and AA was added to the obtained mixed syrup 2 to obtain a mixed syrup 3 having a polymer concentration of 9.0%.

(Preparation of mixed syrup 4 by partial polymerization method)
In the preparation of mixed syrup 1, mixed syrup 4 having a partially polymerized polymer concentration of 36.0% was obtained by the same operation as the preparation of syrup 1, except that the polymerization initiation temperature was 100 ° C. The weight average molecular weight of the produced polymer was 520,000.

(Preparation of mixed syrup 5 by partial polymerization method)
In the preparation of the mixed syrup 4, a mixed monomer solution consisting of 2EHA having the same composition and AA was added to the obtained mixed syrup 2 to obtain a mixed syrup 5 having a polymer concentration of 7.3%.

(Preparation of mixed syrup 6 by solution polymerization method)
For 100 parts by weight of a mixed monomer solution consisting of 90 parts by weight of 2EHA as an ethylenically unsaturated monomer and 10 parts by weight of AA as a polar monomer, thioglycolic acid (manufactured by Sakai Chemical Industry Co., Ltd., trade name “ Mercaptoacetic acid ") 0.2 parts by weight, 2,2'-azobisisobutyronitrile (made by Kishida Chemical Co., Ltd., trade name" AIBN ") 0.2 parts by weight as a polymerization initiator, and 67 parts by weight of ethyl acetate as a solvent The solution was poured into a four-necked flask and heated in a hot water bath at 60 ° C. for 4 hours and further at 70 ° C. for 3 hours in a nitrogen atmosphere to obtain a polymer solution having a polymer concentration of about 60%. The obtained polymer solution was washed several times with methanol to obtain a polymer having a weight average molecular weight of 180,000. The obtained polymer was dissolved in a mixed monomer solution consisting of 90 parts by weight of 2EHA and 10 parts by weight of AA as a polar monomer to obtain a mixed syrup 6 having a polymer concentration of 10.0%.

(Preparation of mixed syrup 7 by solution polymerization method)
In the preparation of the mixed syrup 6, the obtained polymer was dissolved in a mixed monomer solution containing 90 parts by weight of 2EHA and 10 parts by weight of AA as a polar monomer to obtain a mixed syrup 7 having a polymer concentration of 20.0%.

(Preparation of mixed syrup 8 by solution polymerization method)
In the preparation of mixed syrup 6, a polymer having a weight average molecular weight of 110,000 was obtained in the same manner as in the preparation of mixed syrup 6, except that 0.4 parts by weight of thioglycolic acid was used as a chain transfer agent. The obtained polymer was dissolved in a mixed monomer solution consisting of 90 parts by weight of 2EHA and 10 parts by weight of AA as a polar monomer to obtain a mixed syrup 8 having a polymer concentration of 10.0%.

(Preparation of mixed syrup 9 by solution polymerization method)
In the preparation of the mixed syrup 8, the obtained polymer was dissolved in a mixed monomer solution consisting of 90 parts by weight of 2EHA and 10 parts by weight of AA as a polar monomer to obtain a mixed syrup 7 having a polymer concentration of 20.0%.

(Preparation of mixed syrup 10 by solution polymerization method)
In the preparation of the mixed syrup 8, the obtained polymer was dissolved in a mixed monomer solution consisting of 90 parts by weight of 2EHA and 10 parts by weight of AA as a polar monomer to obtain a mixed syrup 7 having a polymer concentration of 30.0%.

(Preparation of mixed syrup 11 by solution polymerization method)
In the preparation of mixed syrup 6, a polymer having a weight average molecular weight of 55,000 was obtained in the same manner as the preparation of mixed syrup 6, except that 1.0 part by weight of thioglycolic acid was used as a chain transfer agent. The obtained polymer was dissolved in a mixed monomer solution consisting of 90 parts by weight of 2EHA and 10 parts by weight of AA as a polar monomer to obtain a mixed syrup 11 having a polymer concentration of 10.0%.

(Preparation of mixed syrup 12 by solution polymerization method)
In the preparation of the mixed syrup 11, the obtained polymer was dissolved in a mixed monomer solution consisting of 90 parts by weight of 2EHA and 10 parts by weight of AA as a polar monomer to obtain a mixed syrup 12 having a polymer concentration of 20.0%.

(Preparation of mixed syrup 13 by solution polymerization method)
In the preparation of the mixed syrup 11, the obtained polymer was dissolved in a mixed monomer solution consisting of 90 parts by weight of 2EHA and 10 parts by weight of AA as a polar monomer to obtain a mixed syrup 13 having a polymer concentration of 40.0%.

(Example 1) To 1,100 parts by weight of mixed syrup, 30 parts by weight of 1,9-nonanediol diacrylate (manufactured by Osaka Organic Chemical Industry Co., Ltd., trade name: Biscote # 260), diphenyl (2,4,6-trimethyl) Benzoyl) phosphine oxide (BASF, trade name; Lucillin TPO) 0.5 parts by weight, 2-hydroxy-2-cyclohexylacetophenone (Ciba Japan, trade name; Irgacure 184) 0.1 parts by weight are uniformly mixed and continuously An oil phase component (hereinafter referred to as “oil phase”) was used. On the other hand, an emulsifier in which 612 parts by weight of ion-exchanged water is added as a co-continuous or discontinuous phase component (hereinafter referred to as “water phase”) to 100 parts by weight of the oil phase component at room temperature. Were continuously added dropwise to a stirring mixer to form a stable water-in-oil type HIPE. The weight ratio of the water phase to the oil phase was 86/14.

  The obtained water-in-oil type HIPE emulsion was applied on a substrate subjected to various peeling treatments so as to have a thickness of 300 μm after light irradiation, and was continuously molded. Further, a polyethylene terephthalate film having a thickness of 38 μm and subjected to a release treatment was placed thereon. This sheet was irradiated with ultraviolet light having a light illuminance of 5 mW / cm 2 (measured with Topcon UVR-T1 having a peak sensitivity maximum wave of 350 nm) using a black light (15 W / cm) to obtain a highly hydrous crosslinked polymer having a thickness of 300 μm. Next, the top film was peeled off, and the high water content crosslinked polymer was heated at 130 ° C. for 10 minutes to obtain a crosslinked foam sheet having a closed cell structure having a thickness of about 300 μm.

(Example 2) A stable water-in-oil type HIPE emulsion was formed in the same manner as in Example 1 except that the mixed syrup 3 was used instead of the mixed syrup 1 in Example 1. From the obtained water-in-oil HIPE emulsion, a crosslinked foam sheet having a closed cell structure having a thickness of about 300 μm was obtained in the same manner as in Example 1.

(Example 3) A stable water-in-oil type HIPE emulsion was formed in the same manner as in Example 1 except that the mixed syrup 5 was used instead of the mixed syrup 1 in Example 1. From the obtained water-in-oil HIPE emulsion, a crosslinked foam sheet having a closed cell structure having a thickness of about 300 μm was obtained in the same manner as in Example 1.

(Example 4) A stable water-in-oil type HIPE emulsion was formed in the same manner as in Example 1 except that the mixed syrup 2 was used instead of the mixed syrup 1 in Example 1. From the obtained water-in-oil HIPE emulsion, a crosslinked foam sheet having a closed cell structure having a thickness of about 300 μm was obtained in the same manner as in Example 1.

Example 5 A stable water-in-oil type HIPE emulsion was formed in the same manner as in Example 1 except that the mixed syrup 4 was used instead of the mixed syrup 1 in Example 1. From the obtained water-in-oil HIPE emulsion, a cross-linked foam sheet having a closed cell structure in which a slight opening was seen in a cell wall having a thickness of about 300 μm was obtained by the same operation as in Example 1.

(Example 6) A stable water-in-oil type HIPE emulsion was formed in the same manner as in Example 1 except that the mixed syrup 6 was used instead of the mixed syrup 1 in Example 1. From the obtained water-in-oil HIPE emulsion, a crosslinked foam sheet having an open cell structure with a thickness of about 300 μm was obtained in the same manner as in Example 1.

(Example 7) A stable water-in-oil type HIPE emulsion was formed in the same manner as in Example 1 except that the mixed syrup 8 was used instead of the mixed syrup 1 in Example 1. From the obtained water-in-oil HIPE emulsion, a crosslinked foam sheet having an open cell structure with a thickness of about 300 μm was obtained in the same manner as in Example 1.

(Example 8) A stable water-in-oil type HIPE emulsion was formed in the same manner as in Example 1 except that the mixed syrup 7 was used instead of the mixed syrup 1 in Example 1. From the obtained water-in-oil HIPE emulsion, a cross-linked foam sheet having an open cell structure in which a large number of openings are seen in the cell wall of fine cells having a thickness of about 300 μm is obtained by the same operation as in Example 1. It was.

(Example 9) A stable water-in-oil type HIPE emulsion was formed in the same manner as in Example 1 except that the mixed syrup 9 was used instead of the mixed syrup 1 in Example 1. From the obtained water-in-oil HIPE emulsion, a crosslinked foam sheet having an open cell structure with a thickness of about 300 μm was obtained in the same manner as in Example 1.

(Example 10) A stable water-in-oil type HIPE emulsion was formed in the same manner as in Example 1 except that the mixed syrup 10 was used instead of the mixed syrup 1 in Example 1. From the obtained water-in-oil HIPE emulsion, a crosslinked foam sheet having an open cell structure with a thickness of about 300 μm was obtained in the same manner as in Example 1.

(Comparative Example 1) In Example 1, except that the mixed syrup 11 was used instead of the mixed syrup 1, an attempt was made to form a water-in-oil type HIPE emulsion by the same operation as in Example 1, but during the emulsification process The phase transition from W / O to O / W was not able to obtain the desired emulsion.

(Comparative Example 2) A water-in-oil type HIPE emulsion was formed in the same manner as in Example 1 except that the mixed syrup 12 was used instead of the mixed syrup 1 in Example 1. The generation of free water that partially separated the oil phase and the aqueous phase was confirmed. From the obtained water-in-oil HIPE emulsion, a crosslinked foam sheet having a semi-independent semi-open cell structure having a thickness of about 300 μm was obtained by the same operation as in Example 1, but the bubble diameters varied. .

(Comparative Example 3) A water-in-oil type HIPE emulsion was formed in the same manner as in Example 1 except that the mixed syrup 13 was used instead of the mixed syrup 1 in Example 1. The generation of free water that partially separated the oil phase and the aqueous phase was confirmed. After forming the water-in-oil type HIPE emulsion, it was immediately applied to form a water-in-oil type emulsion and immediately irradiated with ultraviolet rays to obtain a high water content crosslinked polymer having a thickness of 200 μm. Next, the top film was peeled off, and the high water content crosslinked polymer was heated at 130 ° C. for 10 minutes to obtain a crosslinked foam sheet having an open cell structure of about 200 μm in thickness. Many through holes (pinholes) were formed in the sheet.

(Comparative Example 4) In Example 1, a water-in-oil type HIPE emulsion was formed by the same operation as in Example 1 except that 100 parts by weight of the polymerizable monomer composition having the same composition was used instead of the mixed syrup. Attempts were made to separate the oil phase from the water phase simultaneously with the addition of the water phase, and the desired water-in-oil emulsion could not be obtained.

(Test evaluation)
The test pieces obtained in the above examples and comparative examples were tested for foamability. The results are shown in Table 1.

(Molecular weight) The weight average molecular weight (Mw) can be measured by gel permeation chromatography (GPC). More specifically, as a GPC measurement device, the product name “HLC-8020GPC” (manufactured by Tosoh Corporation) can be used to measure and obtain the value in terms of polystyrene under the following GPC measurement conditions.
GPC measurement conditions and sample concentration: 0.1% by weight (tetrahydrofuran solution)
Sample injection volume: 100 μl
・ Eluent: Tetrahydrofuran (THF)
・ Flow rate (flow rate): 0.5 mL / min
Column temperature (measurement temperature): 40 ° C
Column: Trade name “TSKgel GMH _HR- H (20)” (manufactured by Tosoh Corporation)
・ Detector: Differential refractometer

(Stability of storage of the emulsion at rest) About 30 g of the water-in-oil emulsion prepared in the emulsification process is weighed into a container with a capacity of 50 ml, and released after 30 minutes, 1 hour, 2 hours and 4 hours after the emulsification process. The state of water generation was observed to evaluate the storage stability at room temperature. ◎: No free water after 4 hours, ○: Slight free water is seen after 2 hours, △; Slight free water is seen after 1 hour, ×: Free water is seen within 30 minutes, or oil Formation of water-in-water emulsion is impossible

(Measurement of average cell diameter) A foam sample prepared by cutting in the thickness direction with a microtome cutter was used as a measurement sample. The cut surface of the measurement sample was photographed with a scanning electron microscope (Hitachi, S-4800) at 800 times or 1200 times. And the bubble diameter of the bubble of the arbitrary range was measured using the image | photographed image, and the average bubble diameter was computed from the measured value.

The evaluation results described above are also shown in Tables 1 to 3 below.

Claims (12)

A water-in-oil emulsion containing the following components (a) and (b) and no emulsifier:
(A) i) a polymerizable monomer composition comprising an ethylenically unsaturated monomer and at least one polar monomer copolymerizable with the ethylenically unsaturated monomer, ii) an ethylenically unsaturated monomer and the ethylenically unsaturated monomer A weight average molecular weight of at least one polymer obtained by polymerizing at least one polar monomer copolymerizable with a saturated monomer and having a weight average molecular weight of 100,000 to 10,000,000, and 5% by weight with respect to the total amount of i) % Of a polymer, iii) a continuous oil phase component comprising at least one polymerization initiator, and iv) at least one crosslinker; and (b) at least one immiscible with the continuous oil phase component Co-continuous or discontinuous phase components. The ethylenically unsaturated monomer of i) and the ethylenically unsaturated monomer of ii) are both at least one alkyl (meth) acrylate having 1 to 20 carbon atoms in the alkyl group,
i) The ratio of at least one alkyl (meth) acrylate having 1 to 20 carbon atoms in the alkyl group to at least one polar monomer copolymerizable with the alkyl (meth) acrylate is 70 to 98. 2 to 30 parts by weight,
The ratio of at least one alkyl (meth) acrylate having 1 to 20 carbon atoms in the alkyl group in ii) to at least one polar monomer copolymerizable with the alkyl (meth) acrylate is 70 to 95. The water-in-oil emulsion according to claim 1, wherein the water-in-oil emulsion is 5 to 30 parts by weight. 70 to 95 parts by weight of 5 to 70 parts by weight of at least one alkyl (meth) acrylate having 1 to 20 carbon atoms in the alkyl group and at least one polar monomer copolymerizable with the alkyl (meth) acrylate The partial composition of the polymerizable composition comprising 30 parts by weight is obtained by adjusting the ratio of unpolymerized monomers to 70 to 98 parts by weight to 2 to 30 parts by weight. Water-in-oil emulsion. The water-in-oil emulsion according to any one of claims 1 to 3, wherein the weight average molecular weight of the ii) polymer is 100,000 or more and 500,000 or less. The water-in-oil emulsion according to any one of claims 1 to 4, wherein the ii) polymer is 20% by weight or more based on the total amount with the i). The amount of the crosslinking agent in the continuous oil phase component is 5 to 30 parts by weight with respect to 100 parts by weight of the mixed syrup of i) and ii) according to any one of claims 1 to 5. Water-in-oil emulsion. The water-in-oil emulsion according to any one of claims 1 to 6, wherein the co-continuous or discontinuous phase component is water. 8. A water-in-oil emulsion according to any one of claims 1 to 7, wherein the co-continuous or discontinuous phase component comprises at least 74 volume percent of the total emulsion. A method for preparing a water-in-oil emulsion comprising:
(a) i) at least one alkyl (meth) acrylate having 1 to 20 carbon atoms in the alkyl group and at least one polar monomer copolymerizable with the alkyl (meth) acrylate, 70 to 95 weight A step of partially polymerizing a polymerizable composition comprising 5 to 30 parts by weight and then adjusting the proportion of unpolymerized monomer to 70 to 98 parts by weight to 2 to 30 parts by weight to obtain a prepolymer syrup;
iii) mixing the prepolymer syrup with at least one polymerization initiator and at least one crosslinking agent to obtain a continuous oil phase component; and
(b) mixing the continuous oil phase component with the immiscible at least one co-continuous or discontinuous phase component without adding an emulsifier;
A preparation method comprising: A method for producing a foam sheet, comprising:
(a) preparing and shaping the water-in-oil emulsion according to any one of claims 1 to 8;
(b) exposing the water-in-oil emulsion to thermal energy, far-infrared rays, ultraviolet rays, or visible light capable of activating the polymerization initiator in the water-in-oil emulsion to form a water-containing crosslinked polymer; and
(c) dehydrating the water-containing crosslinked polymer,
The manufacturing method of the foam sheet containing this. The process of (a) preparing and forming the water-in-oil emulsion, (b) forming the hydrous crosslinked polymer, and (c) dehydrating the hydrous crosslinked polymer are performed continuously. The manufacturing method of the foam sheet of description. A foam sheet obtained from the water-in-oil emulsion according to any one of claims 1 to 8, and having an open-cell structure having an average cell diameter of 20 µm or less and an opening between the cells.

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