JP2018087276A - Composite particle, method for producing the same, and oil-water separation material comprising the same - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a particle having extreme high lipophilic and water-repellent properties.SOLUTION: A composite particle contains a condensate obtained by condensing a fluoroalkyl group-containing oligomer having an alkoxysilyl group, and an isocyanate compound-crosslinked cyclodextrin polymer. Suitably, the composite particle has an average particle size of 0.01 μm or more and 100 μm or less. The present invention also provides a method for producing the composite particle, and an oil-water separation material comprising the composite particle.SELECTED DRAWING: None

Description

  The present invention relates to composite particles and a method for producing the same. The present invention also relates to an oil / water separator and an organic compound adsorbent using the composite particles.

  Fluorine compounds can be expected to be applied to paints, cosmetics, etc. by taking advantage of features such as water / oil repellency, oxygen permeability and low refractive index. However, since fluorine compounds have too high water and oil repellency, it is difficult to maintain dispersion stability with respect to non-fluorine raw materials.

  In addition, fluorine compounds that exhibit high oil repellency in air have the disadvantage that the oil repellency disappears in water and the oil spreads wet.

  Wastewater containing oil is a major cause of environmental pollution and is required to be treated appropriately. Conventionally, methods such as stationary separation such as specific gravity separation, centrifugal separation, and adsorption separation are used for oil-water separation treatment.

  However, stationary separation requires a lot of time, centrifugation requires a large-scale apparatus, and adsorption separation is unsuitable for processing a large amount of oil-water mixture.

  The present inventors have previously proposed various new functional materials using a fluoroalkyl group-containing oligomer and imparting excellent characteristics resulting from the fluoroalkyl group-containing oligomer (for example, Patent Documents 1 to 3) reference).

  In addition, the present inventors previously obtained a nanocomposite obtained by a sol-gel reaction under alkaline or acidic conditions of a fluoroalkyl group-containing oligomer having an alkoxysilyl group in the presence of 4,4′-diphenylmethane diisocyanate. Particles were proposed (see Non-Patent Document 1).

JP 2010-209300 A JP 2010-235943 A JP2013-185071A

Proceedings of the Chemical Society of Japan, Vol.95th, No.3, Page1007 (2015)

  For example, when the mixed solution contains a large amount of oil or contains a highly useful oil, it may be advantageous for the user to use only water or a type in which only oil passes through the oil-water separator. This type of oil-water separator is required to be excellent in hydrophilicity and oil repellency, or excellent in lipophilicity and water repellency. Although the nanocomposite particles described in Non-Patent Document 1 are excellent in water repellency, particles excellent in super oleophilicity and super water repellency have not yet been obtained.

  Accordingly, an object of the present invention is to provide composite particles excellent in super-lipophilicity and super-water repellency that can be suitably used as an oil / water separator, an industrially advantageous production method thereof, and an oil / water separator using the composite particles. Is to provide.

  In the course of developing a new functional material using a fluoroalkyl group-containing oligomer, the present inventors include a condensate obtained by condensing a specific fluoroalkyl group-containing oligomer and an isocyanate compound-crosslinked cyclodextrin polymer. It has been found that the composite particles have super lipophilicity and super water repellency and can be suitably used as an oil / water separator, and the present invention has been completed.

  That is, the first invention to be provided by the present invention is a condensate obtained by condensing a fluoroalkyl group-containing oligomer having an alkoxysilyl group represented by the following general formula (1), and an isocyanate compound-crosslinked cyclodextrin polymer. Is a composite particle containing

In the formula, R ¹ and R ² represent a — (CF ₂ ) pY group, or a —CF (CF ₃ ) — [OCF ₂ CF (CF ₃ )] q—OC ₃ F ₇ group, and R ¹ and R ² may be the same group or different groups.
Y represents a hydrogen atom, a fluorine atom or a chlorine atom, and p and q are each independently an integer of 0 or more and 10 or less.
R ³ , R ⁴ and R ⁵ represent a linear or branched alkyl group having 1 to 5 carbon atoms, and R ³ , R ⁴ and R ⁵ may be the same group or different groups. May be.
m is an integer of 2-3.

  Further, the second invention to be provided by the present invention is a condensation product obtained by condensing a fluoroalkyl group-containing oligomer having an alkoxysilyl group represented by the following general formula (1), and an isocyanate compound-crosslinked cyclodextrin polymer. Is a method for producing composite particles having a reaction step in which an alkali is added to a reaction raw material solution containing, to carry out a hydrolysis reaction of the alkoxysilyl group.

In the formula, R ¹ and R ² represent a — (CF ₂ ) pY group, or a —CF (CF ₃ ) — [OCF ₂ CF (CF ₃ )] q—OC ₃ F ₇ group, and R ¹ and R ² may be the same group or different groups.
Y represents a hydrogen atom, a fluorine atom or a chlorine atom, and p and q are each independently an integer of 0 or more and 10 or less.
R ³ , R ⁴ and R ⁵ represent a linear or branched alkyl group having 1 to 5 carbon atoms, and R ³ , R ⁴ and R ⁵ may be the same group or different groups. May be.
m is an integer of 2-3.

  The third invention to be provided by the present invention is an oil / water separator using the composite particles of the first invention.

According to the present invention, composite particles having super lipophilicity and super water repellency can be provided. The composite particles can be suitably used as an oil-water separator that separates water and oil.
Further, according to the present invention, the composite particles can be provided by an industrially advantageous method.

FIG. 1 is a schematic view showing one embodiment of oil / water separation using the oil / water separator of the present invention. FIG. 2 is a schematic view showing one embodiment in which oil / water separation is performed using the oil / water separator of the present invention.

  Hereinafter, the present invention will be described based on preferred embodiments thereof. The composite particle according to the present invention includes a condensate obtained by condensing a fluoroalkyl group-containing oligomer having an alkoxysilyl group represented by the general formula (1) (hereinafter also referred to as “fluoroalkyl group-containing oligomer”). And an isocyanate compound-crosslinked cyclodextrin polymer.

  The composite particles according to the present invention contain 5 parts by mass or more and 500 parts by mass or less, particularly 10 parts by mass or more and 200 parts by mass or less, of an isocyanate compound-crosslinked cyclodextrin polymer with respect to 100 parts by mass of the condensate of fluoroalkyl group-containing oligomer. It is preferable from the viewpoint of developing super lipophilicity and super water repellency.

  The composite particles of the present invention preferably have an average particle size of 0.01 μm to 100 μm, more preferably 0.1 μm to 70 μm. When the average particle diameter is within this range, dispersibility in various dispersion solvents, resin materials, various base materials, and the like is improved. The average particle diameter can be determined by a laser diffraction scattering method, and can be measured by using, for example, a laser diffraction particle size distribution measuring apparatus (SALD-300V manufactured by Shimadzu Corporation).

  The composite particles of the present invention preferably have a structure in which particles of a condensate of a fluoroalkyl group-containing oligomer having a smaller diameter than the particles are dispersed on the surface of the isocyanate compound-crosslinked cyclodextrin polymer particles. . The particles of the condensate of the fluoroalkyl group-containing oligomer are preferably uniformly dispersed on the surface of the isocyanate compound-crosslinked cyclodextrin polymer particles that are the core material. “Uniformly dispersed” means that (i) particles of a condensate of a fluoroalkyl group-containing oligomer are arranged sparsely and uniformly so that the surface of the isocyanate compound-crosslinked cyclodextrin polymer particles that are the core material is exposed. And (ii) when the particles of the condensation product of the fluoroalkyl group-containing oligomer are densely and uniformly arranged so that the surface of the isocyanate compound crosslinked cyclodextrin polymer particles that are the core material is not exposed. Both of the dispersion states are included. From the viewpoint that the composite particles of the present invention easily express super-lipophilicity and super-water repellency, the condensate particles of the fluoroalkyl group-containing oligomer are formed on the surface of the isocyanate compound-crosslinked cyclodextrin polymer particles as the core material. , (I) is preferably dispersedly arranged.

  The composite particle according to the present invention is a reaction in which an alkali is added to a reaction raw material solution containing a condensate obtained by condensing a fluoroalkyl group-containing oligomer and an isocyanate compound-crosslinked cyclodextrin polymer, and a hydrolysis reaction of the alkoxysilyl group is performed. It is preferable that it is obtained by a process.

The fluoroalkyl group-containing oligomer is represented by the general formula (1) and has a hydrolyzable alkoxysilyl group. Examples of the linear or branched alkyl group having 1 to 5 carbon atoms represented by R ³ , R ⁴ and R ⁵ in the general formula (1) include a methyl group, an ethyl group, a propyl group, a butyl group, and A pentyl group etc. are mentioned.

In the general formula (1), R ¹ and R ² — (CF ₂ ) pY group, or —CF (CF ₃ ) — [OCF ₂ CF (CF ₃ )] q—OC ₃ F ₇ group p and q is each independently an integer of 0 or more and 10 or less, preferably each independently an integer of 0 or more and 3 or less. In particular, R ¹ and R ² are preferably —CF (CF ₃ ) OC ₃ F ₇ .

  The fluoroalkyl group-containing oligomer represented by the general formula (1) is produced, for example, by reacting a trialkoxyvinylsilane such as trimethoxyvinylsilane with a fluoroalkanoyl peroxide (for example, JP-A-2002-338691 and (See JP 2010-77383 A). The resulting fluoroalkyl group-containing oligomer is nano-sized fine particles.

  The isocyanate compound-crosslinked cyclodextrin polymer contained in the composite particles according to the present invention imparts excellent lipophilicity and excellent oil / water separation ability to the composite particles of the present invention.

The isocyanate compound-crosslinked cyclodextrin polymer has a structure in which —OH groups and CH ₂ OH groups in cyclodextrin are crosslinked with an isocyanate compound. The crosslinking site includes, for example, a urethane bond. The isocyanate compound cross-linked cyclodextrin polymer is preferably water-insoluble.

  Examples of the cyclodextrin that is a target compound that is cross-linked by an isocyanate compound include α-cyclodextrin that is a six-membered ring compound, β-cyclodextrin that is a seven-membered ring compound, and γ-cyclodextrin that is an eight-membered ring compound. It has been known. In the present invention, these cyclodextrins can be used without particular limitation. One cyclodextrin polymer may be composed of one type of cyclodextrin, or may be composed of two or more types of cyclodextrin.

  As an isocyanate type compound used in order to bridge | crosslink cyclodextrin, an aromatic isocyanate type compound, an aliphatic isocyanate type compound, and a cyclic aliphatic isocyanate type compound are mentioned, for example. These isocyanate compounds are preferably diisocyanate compounds. In particular, an aromatic diisocyanate compound and an aliphatic diisocyanate compound are preferable.

  Specific examples of the isocyanate compound include toluene diisocyanate, naphthalene diisocyanate such as 1,5-naphthalene diisocyanate, diphenylmethane diisocyanate such as 4,4′-diphenylmethane diisocyanate, 4,4′-diphenyldimethylmethane diisocyanate, 4,4′- Dibenzyl diisocyanate, tetraalkyldiphenylmethane diisocyanate, 1,3-phenylene diisocyanate, 1,4-phenylene diisocyanate, 2,6-tolylene diisocyanate, 2,4-tolylene diisocyanate, butane-1,4-diisocyanate, hexamethylene diisocyanate 2,2,4-trimethylhexamethylene diisocyanate, 2,4,4-trimethylhexamethylene diisocyanate, Rohekisan-1,4-diisocyanate, xylylene diisocyanate, isophorone diisocyanate, dicyclohexylmethane-4,4'-diisocyanate, 1,3-bis (isocyanatomethyl) cyclohexane, methylcyclohexane diisocyanate, and derivatives thereof. These isocyanate compounds can be used alone or in combination of two or more.

  Particularly preferred isocyanate-based compounds include, but are not limited to, toluene diisocyanate, diphenylmethane diisocyanate, naphthalene diisocyanate, xylylene diisocyanate, isophorone diisocyanate and hexamethylene diisocyanate.

  The use range of the cyclodextrin and the isocyanate compound is not particularly limited, but it is preferably used in the range of 1 mol or more and 24 mol or less of the isocyanate compound with respect to 1 mol of the cyclodextrin. More preferably, the amount of the isocyanate compound is 2 mol or more and 16 mol or less, more preferably 6 mol or more and 12 mol or less with respect to 1 mol of cyclodextrin.

  The reaction between the cyclodextrin and the isocyanate compound is preferably performed in a temperature range of, for example, 30 ° C. or more and 150 ° C. or less, particularly 50 ° C. or more and 100 ° C. or less. On the condition of this temperature range, the reaction time is preferably 0.5 hours or more and 24 hours or less. The reaction can be carried out in a solvent or without a solvent.

  When the reaction is performed using a solvent, an organic solvent that does not affect the reaction is preferably used as the solvent. Such solvents include, for example, dialkylformamides such as dimethylformamide and diethylformamide, dialkyl sulfoxides such as dimethyl sulfoxide and diethyl sulfoxide, aliphatic nitriles and aromatic nitriles such as acetonitrile and benzonitrile, pyridine and n- Aromatic and aliphatic amines such as butylamine, aliphatic ethers such as dimethyl ether and diethyl ether, cyclic ethers such as dioxane, and aromatic hydrocarbons such as benzene, toluene and xylene. In consideration of stability and solubility, it is preferable to use dialkyl formaldehydes and dialkyl sulfoxides.

  The isocyanate compound cross-linked cyclodextrin polymer obtained as described above preferably has an average particle size of 0.01 μm or more and 500 μm or less, and more preferably 0.1 μm or more and 40 μm or less.

  Examples of the reaction solvent used when producing the composite particles according to the present invention include those capable of dissolving the fluoroalkyl group-containing oligomer. Specific examples of the reaction solvent include lower alcohols such as methanol, ethanol and isopropyl alcohol, which may be used alone or in combination of two or more. Of these, methanol is particularly preferred.

  The content of the isocyanate compound-crosslinked cyclodextrin polymer in the reaction raw material solution is preferably 5 parts by mass or more and 500 parts by mass or less, and more preferably 10 parts by mass or more and 200 parts by mass or less. On the condition that the content of the isocyanate-based compound-crosslinked cyclodextrin polymer is within this range, the content of the fluoroalkyl group-containing oligomer represented by the general formula (1) is 5 parts by mass or more and 500 parts by mass or less. It is preferably 10 parts by mass or more and 250 parts by mass or less. When the contents of both in the reaction raw material solution are within this range, the composite particles of the present invention exhibit super lipophilicity and super water repellency.

  In the reaction step, the alkali added to the reaction raw material solution is not particularly limited as long as it can hydrolyze alkoxysilane, and examples thereof include ammonium hydroxide, sodium hydroxide, and potassium hydroxide. Of these, ammonium hydroxide is preferably used because of its high reactivity.

  The amount of alkali added to the reaction raw material solution is not particularly limited and is appropriately selected. Moreover, the reaction temperature at the time of reacting by mixing an alkali with a reaction raw material solution becomes like this. Preferably they are -5 degreeC or more and 50 degrees C or less, More preferably, they are 0 degreeC or more and 30 degrees C or less. By setting the reaction temperature to −5 ° C. or higher, the hydrolysis rate of the alkoxysilyl group can be prevented from being excessively slow, and sufficient reaction efficiency can be obtained. By setting the reaction temperature to 50 ° C. or lower, composite particles An excessive decrease in dispersion stability can be suppressed. The reaction time for carrying out the reaction by mixing an alkali with the reaction raw material solution is not particularly limited and is appropriately selected, but is preferably 1 hour or longer and 72 hours or shorter, and particularly preferably 1 hour or longer and 24 hours or shorter.

  As for the said reaction, sufficient reaction efficiency is obtained by stirring a liquid if necessary. Further, by stirring the liquid during the reaction, fine composite particles, for example, composite particles having an average particle diameter of preferably 0.01 μm or more and 100 μm or less, and more preferably 0.1 μm or more and 70 μm or less can be obtained. .

  After completion of the reaction, the precipitate is filtered by a conventional method, and then purified by washing, drying or the like as necessary to obtain the desired composite particles.

  The composite particles obtained by the above method can be used as, for example, an oil / water separator. Specifically, using the composite particles of the present invention as an oil / water separator, water and oil can be separated by bringing the oil / water separator into contact with a mixed liquid containing water and oil.

The composite particles of the present invention can be used as an oil-water separator by, for example, the following two methods.
(A) A method of modifying a water-insoluble substrate with the composite particles of the present invention.
(B) A method of using the composite particles of the present invention as they are as a filtering material.

  As a base material which concerns on said (A), the inorganic substance and organic substance which are insoluble in water can be used. Examples of the inorganic substance include glass fiber, silica, silica gel, alumina, slag wool, molecular sieve, zeolite, activated carbon, diatomaceous earth, sand, asbestos and the like. The organic substance may be a natural polymer or a synthetic polymer. Examples of the natural polymer include cellulose, wool, cotton, silk and the like. Examples of synthetic polymers include condensation-type or addition-type polymer polymers such as polyurethane, polyethylene terephthalate, nylon, and polycarbonate, and ethylenically unsaturated polymer polymers such as polyethylene, polypropylene, vinyl chloride, and vinyl acetate. It is done.

  The shape of the substrate is not particularly limited, and examples include strips, sponges, ribbons, fibrils, webs, mats, cottons, and nonwovens.

  In the present invention, a commercially available filter paper or the like may be used as a base material for modifying. In this case, the pore diameter of the filter paper is preferably 5 μm or less, more preferably 0.1 μm or more and 3 μm or less from the viewpoint of efficient oil-water separation.

  In (A), the method for modifying the base material with the composite particles of the present invention is not particularly limited as long as the composite particles of the present invention can be fixed or supported on the surface or inside of the base material. A known method can be used. For example, there is a method in which the substrate is brought into contact with a dispersion in which the composite particles of the present invention are dispersed at a concentration of 1% by mass or more and 50% by mass or less, and then dried. Further, the contact between the dispersion and the substrate can be performed by a method of immersing the substrate in the dispersion, a method of spraying the substrate by spraying, a method of applying the dispersion to the substrate, or the like.

  FIG. 1 is a schematic view showing an embodiment in the case where a mixed solution of water and oil is separated using a filter paper modified with the composite particles of the present invention. The separation system A of the embodiment shown in the figure includes a modified filter paper 1a and a column 1b. The modified filter paper 1a is a filter paper modified with the composite particles of the present invention.

  By interposing the modified filter paper 1a in the middle of the column 1b, the mixed liquid 1 of water and oil charged into the column 1b comes into contact with the modified filter paper 1a. Oil 1 'passes through the modified filter paper 1a, while water cannot pass through the modified filter paper 1a, so that water and oil can be separated. In order to increase the separation efficiency as necessary, it is possible to apply pressure or reduce the pressure during the separation operation. In this case, first, the oil 1 'may selectively pass through the modified filter paper 1a, and then water may pass through the modified filter paper with a delay due to strong external force. And after oil 1 'elutes, water and oil can be separated through an oil-water separator by means such as finishing the oil-water separation operation.

  FIG. 2 is a schematic view showing one embodiment in the case where a mixed liquid of water and oil is separated using the composite particles of the present invention as a filter medium. The separation system B of the embodiment shown in the figure includes a filter medium layer 2a including a column 2b and a filter medium 2c.

  The column 2b is filled with the composite particles of the present invention as the filter medium 2c to form the filter medium layer 2a. By introducing the mixed liquid 1 of water and oil into the column 2b, the filter medium 2c and the mixed liquid can be brought into contact with each other. Since the oil 1 'passes through the filter medium layer 2a, water cannot pass through the filter medium layer 2a, so that water and oil can be separated. In order to increase the separation efficiency as necessary, it is possible to apply pressure or reduce the pressure during the separation operation. Moreover, in order to suppress clogging etc., the layer which filled the filter aid in the upper part and / or the lower part of the filter material layer 2a can be provided if needed.

  There is no restriction | limiting in particular as a filter aid which can be used, A well-known thing can be used widely. Examples include diatomaceous earth, sand particles, pearlite, anthracite, cellulose, wool, cotton, silk, carbonaceous filter aid, acid clay, bentonite, celite, talc, mica and kaolinite. These can be used individually by 1 type or in combination of 2 or more types.

  The mixed liquid of water and oil to be treated with the oil / water separator according to the present invention may be in a solution state or an emulsion.

  The oil / water separator according to the present invention can be used for, for example, wastewater treatment containing oil, means for separating or purifying water and oil at production sites in various industrial fields, and the like.

  Hereinafter, the present invention will be described with reference to examples. However, the scope of the present invention is not limited to these examples. Unless otherwise specified, “%” represents “mass%”.

<Preparation of oligomer containing fluoroalkyl group>
The fluoroalkyl group-containing oligomers (hereinafter referred to as “VM”) used in the following Examples and Comparative Examples are shown in Table 1 below. In the same table, the molecular weight represents the number average molecular weight determined by gel permeation chromatography (GPC, polystyrene conversion).

<Preparation of MDI cross-linked β-cyclodextrin polymer>
The MDI (1-isocyanate-4-[(4-isocyanatephenyl) methylbenzene]) cross-linked β-cyclodextrin polymer (hereinafter also referred to as MDI-β-CD polymer) used in the following examples was synthesized by the following method. .
1100 mg of β-cyclodextrin and 2250 mg of MDI were added to 50 ml of dimethylformamide and heated at 70 ° C. for 6 hours to obtain a reaction solution. The reaction solution was added to an excess of tetrahydrofuran to precipitate a solid. After filtration, the solid was stirred and washed overnight with a water / methanol solution having a volume ratio of 1: 1 to obtain an MDI crosslinked β-cyclodextrin polymer sample. Got.

<Average particle size>
The average particle diameter of the composite particles obtained in the following Examples and Comparative Examples was measured with a laser diffraction particle size distribution measuring device (SALD-300V manufactured by Shimadzu Corporation).

<Evaluation of contact angle with dodecane and contact angle with water>
A glass plate was immersed in the reaction solution samples obtained in the following Examples and Comparative Examples for 1 minute at room temperature (25 ° C.). After pulling up the glass plate, it was naturally dried and further vacuum dried at 20 ° C. overnight. With respect to the surface of the modified glass plate thus obtained, the contact angle with dodecane and the contact angle with water were measured using Drop Master.300 manufactured by Kyowa Interface Science. The results are shown in Table 3. In the table, “-” indicates that there was no change in the contact angle.

[Examples 1 to 4]
To a solution obtained by dissolving the amount of VM shown in Table 2 below in 5 ml of methanol, a solution obtained by dissolving the amount of MDI-crosslinked β-cyclodextrin polymer shown in the same table in 1 ml of pure water is added and stirred for 10 minutes with a magnetic stirrer. went. Next, 1 ml of a 25% aqueous ammonia solution was added, and the mixture was stirred at room temperature (25 ° C.) for 5 hours using a magnetic stirrer. After completion of the reaction, the solvent was removed from the reaction solution sample under reduced pressure, then redispersed in methanol, and centrifuged to obtain the target composite particle as a white powder. The average particle size of the obtained composite particles was as shown in Table 2. The obtained composite particles were measured for the contact angle. The results are shown in Table 3 below. In the table, “-” indicates that there was no change in the contact angle.

[Comparative Example 1]
The contact angle was measured for a VM that was not composited with an MDI-crosslinked β-cyclodextrin polymer. The results are shown in Table 3 below. In the table, “-” indicates that there was no change in the contact angle.

  As is clear from the results shown in Tables 2 and 3, the plate glass whose surface was modified by the composite particles of each Example was super-lipophilic and super-water-repellent compared to Comparative Example 1. I understand that.

<Evaluation as oil-water separator>
A chromatographic column (inner diameter: 10 mm) was packed with sea sand so that the layer thickness was about 1 mm. Next, 200 mg (layer thickness: about 4 mm) of each of the composite particles prepared in Example 1 and silica particles (Wakogel (registered trademark) C-500HG) as Comparative Example 2 were filled. Further, sea sand was filled thereon so that the layer thickness was about 1 mm. Using this chromatography column, the performance as an oil / water separator was evaluated by the following procedure.
For the evaluation, an emulsion prepared by mixing 5 ml of 1,2-dichloroethane (DCE), 0.05 ml of water and 20 mg of Span 80 as an emulsifier was used. The oil-water separation of the emulsion was performed by vacuum filtration using the apparatus shown in FIG. The results are shown in Table 4. The recovery rate (%) of DCE in the same table was calculated by the following formula.
DCE recovery rate (%) = [(mass W of recovered DCE) / (mass W _{0 of} DCE used)] × 100
Moreover, the evaluation criteria of oil-water separation in Table 4 are as follows.
○: Water is not visually observed in the filtrate.
Δ: Some water is visually observed in the filtrate.
X: An emulsion is visually observed in the filtrate.

  As is clear from the results shown in Table 4, in Comparative Example 2, the liquid mixture containing water and oil passed through the filtrate as it was immediately after the separation operation, and water and oil could not be separated at all. In contrast, by using the column of Example 1, it can be seen that oil can be recovered from the emulsion in high yield via the composite particles.

DESCRIPTION OF SYMBOLS 1 Mixed liquid 1 'Oil 1a Filter paper 1b Column 2a Filter medium layer 2b Column 2c Filter medium A, B Separation system

Claims (8)

Composite particles containing a condensate obtained by condensing a fluoroalkyl group-containing oligomer having an alkoxysilyl group represented by the following general formula (1) and an isocyanate compound-crosslinked cyclodextrin polymer.

In the formula, R ¹ and R ² represent a — (CF ₂ ) pY group, or a —CF (CF ₃ ) — [OCF ₂ CF (CF ₃ )] q—OC ₃ F ₇ group, and R ¹ and R ² may be the same group or different groups.
Y represents a hydrogen atom, a fluorine atom or a chlorine atom, and p and q are each independently an integer of 0 or more and 10 or less.
R ³ , R ⁴ and R ⁵ represent a linear or branched alkyl group having 1 to 5 carbon atoms, and R ³ , R ⁴ and R ⁵ may be the same group or different groups. May be.
m is an integer of 2-3. The composite particles according to claim ^1, wherein R ¹ and R ² in the general formula (1) are —CF (CF ₃ ) OC ₃ F ₇ .   The composite particle according to claim 1 or 2, wherein the isocyanate compound is toluene diisocyanate, diphenylmethane diisocyanate, naphthalene diisocyanate, xylylene diisocyanate, isophorone diisocyanate or hexamethylene diisocyanate.   The composite particle according to any one of claims 1 to 3, having an average particle diameter of 0.01 µm or more and 100 µm or less. An alkali is added to a reaction raw material solution containing a condensate obtained by condensing a fluoroalkyl group-containing oligomer having an alkoxysilyl group represented by the following general formula (1) and an isocyanate compound-crosslinked cyclodextrin polymer. A method for producing composite particles having a reaction step of hydrolyzing a silyl group.

In the formula, R ¹ and R ² represent a — (CF ₂ ) pY group, or a —CF (CF ₃ ) — [OCF ₂ CF (CF ₃ )] q—OC ₃ F ₇ group, and R ¹ and R ² may be the same group or different groups.
Y represents a hydrogen atom, a fluorine atom or a chlorine atom, and p and q are each independently an integer of 0 or more and 10 or less.
R ³ , R ⁴ and R ⁵ represent a linear or branched alkyl group having 1 to 5 carbon atoms, and R ³ , R ⁴ and R ⁵ may be the same group or different groups. May be.
m is an integer of 2-3. The method for producing composite particles according to claim 5, wherein R ¹ and R ² in the general formula (1) are —CF (CF ₃ ) OC ₃ F ₇ .   The method for producing composite particles according to claim 5 or 6, wherein the isocyanate compound is toluene diisocyanate, diphenylmethane diisocyanate, naphthalene diisocyanate, xylylene diisocyanate, isophorone diisocyanate or hexamethylene diisocyanate.   The oil-water separation material using the composite particle as described in any one of Claims 1 thru | or 4.

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