JP2016019969A - Potting agent for hollow fiber membrane module - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a potting agent for a hollow fiber membrane module where the elution amount of an organic compound component is significantly low, which is cured at a low temperature and whose heat generation is low.SOLUTION: A potting agent for a hollow fiber membrane module comprises: 100 pts.wt. of an epoxy resin having an epoxy equivalent of 230 or less, having an aromatic ring in a molecule and being a liquid at 23°C 0.10 MPa; a main agent including 3-20 pts.wt. of at least one kind of reactive diluents selected from the group consisting of a reactant of a cashew nutshell liquid and epichlorohydrin, mono glycidyl ether having a structure expressed as Formula:(1), 4-tert-butyl phenylglycidyl ether and an epoxidized soybean oil; and a curing agent including at least one kind selected from the group consisting of polyoxyalkylene triamine and polyalkylene diamine and 25-65 pts.wt. of an amine compound having a total amine value of 56-393 and an average functionality of 2.6-3.0.SELECTED DRAWING: None

Description

  The present invention relates to a potting agent for a hollow fiber membrane module.

  In recent years, interest in tap water quality has been increasing. In the conventional flocculation / sand filtration method, there are bacteria and viruses that pass through the gaps in the sand. Therefore, a filtration method using a membrane has attracted attention. Depending on the pore size of the membrane, a general RO membrane, loose RO membrane, ultrafiltration membrane or microfiltration membrane can remove most bacteria and viruses by filtration.

  A hollow fiber membrane module is generally used for the filtration method using a membrane. The hollow fiber membrane module is composed of a hollow fiber membrane bundle in which several hundred to tens of thousands of hollow fiber membranes having selective permeability are aligned and bundled, and a cylindrical storage case for storing the hollow fiber membrane bundle. It is configured. Both ends of the hollow fiber membrane bundle are integrated with the hollow fiber membrane module potting agent filled with a gap between the hollow fiber membranes, and the hollow fiber membrane module potting agent accommodates the hollow fiber membrane bundle. The case is integrated.

  In recent years, a filtration method using the hollow fiber membrane module has begun to be used instead of the sand filtration method mainly in a simple water purification plant.

  In recent years, liquid treatment using a hollow fiber membrane module is not limited to the production of industrial pure water and ultrapure water, but includes various processes such as seawater desalination, drinking water purification, drainage treatment, and beverage concentration. The application is expanding.

  As described above, both ends of the hollow fiber membrane module of the hollow fiber membrane module are fixed and integrated in the housing case with the potting agent for the hollow fiber membrane module, so that the hollow fiber membrane is filtered when filtered water passes through the hollow fiber membrane module. Contact with potting agent for membrane module. Therefore, it is required that the organic compound component does not elute as much as possible from the potting agent for the hollow fiber membrane module.

  Therefore, Patent Document 1 discloses an elution amount of an organic compound component using an epoxy resin as a main agent and an acid anhydride compound as a curing agent in an adhesive sealant used for sealing a plurality of hollow fiber membrane end portions. A method for producing a low hollow fiber membrane module is disclosed.

Japanese Patent Laid-Open No. 3-188927

  However, the hollow fiber membrane module has insufficient prevention of elution of organic compound components, and further improvement is required.

  In the manufacturing process for the hollow fiber membrane module, the adhesive sealant (the potting agent for the hollow fiber membrane module) is cured by heating, but the adhesive sealant requires a high temperature of 150 ° C. (implementation). Example 1) has a problem that the hollow fiber membrane is damaged and the original filtration ability of the hollow fiber membrane is remarkably lowered.

  The present invention provides a potting agent for a hollow fiber membrane module in which the elution amount of an organic compound component is remarkably low, is cured at a low temperature and has low heat generation.

  The potting agent for a hollow fiber membrane module of the present invention comprises 100 parts by weight of an epoxy resin having an epoxy equivalent of 230 or less, having an aromatic ring in the molecule and being liquid at 23 ° C. and 0.10 MPa, and cashew nut shell liquid. At least one reactive dilution selected from the group consisting of a reaction product with epichlorohydrin, monoglycidyl ether having a structure represented by formula (1), 4-tert-butylphenylglycidyl ether and epoxidized soybean oil A main agent containing 3 to 20 parts by weight of the agent, and at least one selected from the group consisting of polyoxyalkylene triamine and polyoxyalkylene diamine, a total amine number of 56 to 393, and an average functionality of 2.6 to 3. And a curing agent containing 25 to 65 parts by weight of an amine compound which is 0

式（１）において、Ｒ¹は、炭素数が８以上のアルキル基である。

In the formula (1), R ¹ is an alkyl group having 8 or more carbon atoms.

  The potting agent for a hollow fiber membrane module is a two-part potting agent containing a main agent and a curing agent, and is used by mixing and curing the main agent and the curing agent. The main component of the potting agent for the hollow fiber membrane module contains an epoxy resin having an aromatic ring. The epoxy resin has an aromatic ring, is cured well at a low temperature of 15 to 40 ° C., and can produce a hollow fiber membrane module without impairing the filtration ability of the hollow fiber membrane. The epoxy resin having an aromatic ring is not particularly limited. For example, bisphenol A type epoxy resin, bisphenol F type epoxy resin, biphenyl type epoxy resin, naphthalene type epoxy resin, phenol novolac type epoxy resin, bisphenol A novolac type epoxy resin, trishydroxymethane type epoxy resin, tetraphenolethane type epoxy resin, tetraglycidyldiaminodiphenylmethane type epoxy resin, aminophenol type epoxy resin, aniline type epoxy resin, benzylamine type epoxy Resin, xylenediamine type epoxy resin and the like, and the elution of the organic compound component is low, the calorific value at the time of curing is low, and the filtration ability of the hollow fiber membrane is not impaired. Epoxy resins are preferred. In addition, an epoxy resin may be used independently or 2 or more types may be used together.

  The epoxy equivalent of the epoxy resin is 230 or less, preferably 160 to 195, more preferably 170 to 195, particularly preferably 184 to 194, since elution of the organic compound component from the cured potting agent can be kept low. preferable. By setting the epoxy equivalent of the epoxy resin to 160 or more, the potting agent for the hollow fiber membrane module is prevented from excessively reacting with the epoxy group per unit volume when the potting agent for the hollow fiber membrane module is cured. A hollow fiber membrane module can be manufactured without suppressing the amount of heat generated during curing and without impairing the filtration ability of the hollow fiber membrane.

  Here, the “epoxy equivalent” is a value obtained by dividing the molecular weight of the epoxy compound by the number of epoxy groups in one molecule. In the present invention, the epoxy equivalent of the epoxy resin refers to a value measured according to JIS K7236.

  The epoxy resin is liquid under conditions of 23 ° C. and 0.10 MPa. Since the epoxy resin is liquid under the conditions of 23 ° C. and 0.10 MPa, the hollow fiber membranes can be firmly integrated with each other without generating a gap between the hollow fiber membranes, and a plurality of hollow The hollow fiber membrane bundle formed by aligning and bundling the yarn membranes is firmly integrated into the storage case constituting the hollow fiber membrane module without causing a gap between the hollow fiber membrane bundle and the storage case. It is possible to manufacture a hollow fiber membrane module that can be used stably over a long period of time.

  The main component of the potting agent for the hollow fiber membrane module contains a reactive diluent. The reactive diluent is a reaction product of cashew nut shell liquid and epichlorohydrin, monoglycidyl ether represented by the structure of formula (1), 4-tert-butylphenylglycidyl ether, and epoxidized soybean oil. Includes at least one selected. These reactive diluents reduce the viscosity of the main agent and reduce the difference between the viscosity of the main agent and the curing agent, thereby facilitating mixing of the main agent and the curing agent, and the potting agent for the hollow fiber membrane module. Improves handling. In addition, the reactive diluent has lower elution of organic compound components than other reactive diluents, and further suppresses the amount of heat generated when the potting agent for hollow fiber membrane module is cured.

式（１）において、Ｒ¹は、炭素数が８以上のアルキル基である。

In the formula (1), R ¹ is an alkyl group having 8 or more carbon atoms.

  The cashew nut shell liquid is also called cashew nut shell oil or cashew nut oil. An oily liquid contained in the shell of cashew nut tree (Anacardium accidentale L., Ursiaceae).

  There are a solvent extraction method and a heating method as methods for collecting cashew nut shell liquid from the husks of cashew nut tree (Anacardium accidentale L., Ursiaceae), and the heating method is mainly used in the production area. That is, the cashew nut shell liquid can be obtained by dry distillation of the cashew nut shell or by solvent extraction directly from the cashew nut shell. As components of cashew nut shell liquid, anacardic acid and cardol are the main components in the extraction method, and cardanol and cardol are the main components in the heating method.

The monoglycidyl ether has a structure of the formula (1) as described above. In the formula (1), R ¹ is an alkyl group having 8 or more carbon atoms because it has moderate hydrophobicity and can reduce the elution of the organic compound component of the potting agent for the hollow fiber membrane module. Since the amount of glycidyl ether used can be reduced and elution of the organic compound component of the potting agent for the hollow fiber membrane module can be reduced, an alkyl group having 11 to 20 carbon atoms is preferable. Examples of R ¹ include linear or branched alkyl groups such as an undecyl group, dodecyl group, tridecyl group, tetradecyl group, pentadecyl group, hexadecyl group, heptadecyl group, octadecyl group, and eicosanyl group.

  The epoxidized soybean oil is a compound epoxidized by oxidizing all or part of unsaturated bonds of a mixed fatty acid mainly composed of fatty acids having unsaturated bonds and soybean oil having a triester structure of glycerin. is there.

  The content of the reactive diluent in the potting agent for the hollow fiber membrane module is 3 to 20 parts by weight, preferably 3 to 18 parts by weight, more preferably 3 to 15 parts by weight with respect to 100 parts by weight of the epoxy resin. 4 to 12 parts by weight is particularly preferable, and 5 to 10 parts by weight is most preferable. When the content of the reactive diluent in the potting agent for the hollow fiber membrane module is 3 parts by weight or more, the viscosity of the main agent of the potting agent for the hollow fiber membrane module decreases, and the viscosity of the main agent and the viscosity of the curing agent are reduced. By reducing the difference, mixing of the main agent and the curing agent is facilitated, and the handleability of the potting agent for the hollow fiber membrane module is improved. When the content of the reactive diluent in the potting agent for hollow fiber membrane modules is 20 parts by weight or less, elution of organic compound components from the potting agent for hollow fiber membrane modules can be reduced.

  The curing agent for the potting agent for the hollow fiber membrane module contains at least one amine compound selected from the group consisting of polyoxyalkylene triamines and polyoxyalkylene diamines. As the polyoxyalkylene triamine, a compound having a structure represented by the formula (2) is preferable.

式（２）において、Ｒ²はメチル基又はエチル基である。Ｒ³はメチル基又はエチル基である。Ｒ⁴はメチル基又はエチル基である。Ｒ⁵はＨ（水素原子）又は炭素数が１〜６のアルキル基である。Ｘ、Ｙ及びＺは正の数である。（Ｘ＋Ｙ＋Ｚ）は５〜６である。

In the formula (2), R ² is a methyl group or an ethyl group. R ³ is a methyl group or an ethyl group. R ⁴ is a methyl group or an ethyl group. R ⁵ is H (hydrogen atom) or an alkyl group having 1 to 6 carbon atoms. X, Y and Z are positive numbers. (X + Y + Z) is 5-6.

In Formula (2), R < ² > -R < ⁴ > is a methyl group or an ethyl group. R ^{2 to} R ⁴ may be the same or different from each other. R ^{2 to} R ⁴ are preferably all methyl groups or R ^{2 to} R ⁴ are preferably all ethyl groups. This is because if the carbon to which the amino group is bonded has a small steric hindrance like the carbon of the methylene chain, the reactivity between the amino group of the polyoxyalkylenetriamine and the epoxy group of the epoxy resin is too high, and the hollow fiber The amount of heat generated when the potting agent for the membrane module is cured increases, which may impair the filtration capacity of the hollow fiber membrane or the storage case of the hollow fiber membrane module. Furthermore, amine brushing is caused by the reaction of the amino group with carbon dioxide in the air, and the elution amount of the organic compound component from the potting agent for the hollow fiber membrane module may increase. On the other hand, when a bulky functional group such as an isopropyl group is bonded to the carbon to which the amino group is bonded, when the potting agent for the hollow fiber membrane module is cured, the amino group of the polyoxyalkylene triamine and the epoxy resin The reaction with the epoxy group does not proceed sufficiently, unreacted products are likely to remain, and the amount of the organic compound component eluted from the potting agent for the hollow fiber membrane module may increase. R ⁵ is H (hydrogen atom) or an alkyl group having 1 to 6 carbon atoms. Examples of the alkyl group having 1 to 6 carbon atoms include a methyl group, an ethyl group, a propyl group, a butyl group, a pentyl group, and a heptyl group.

  In Formula (2), X, Y, and Z are positive numbers, and (X + Y + Z) is 5-6. (X + Y + Z) is a hollow fiber membrane module that can easily produce a hollow fiber membrane module without reducing the amount of heat generated when the potting agent for the hollow fiber membrane module is cured, and impairing the filtration performance of the hollow fiber membrane. The amount of elution of the organic compound component from the potting agent for the hollow fiber membrane module can be reduced by sufficiently crosslinking and curing the potting agent for use.

  A commercial item can be used for the compound represented by Formula (2). The compound represented by the formula (2) is commercially available, for example, from Huntsumman under the trade names “Jeffamine T-403” and “Jeffamine XTJ-566”.

  As the polyoxyalkylene diamine, a compound having a structure represented by the formula (3) is preferable.

In the formula (3), R ⁶ is a methyl group or an ethyl group. R ⁷ is a methyl group or an ethyl group. n is 2-7.

In Formula (3), it is preferable that R ⁶ and R ⁷ are both methyl groups, or R ⁶ and R ⁷ are both ethyl groups. This is because if the carbon to which the amino group is bonded has a small steric hindrance like the carbon of the methylene chain, the reactivity between the amino group of the polyoxyalkylenediamine and the epoxy group of the epoxy resin is too high, and the hollow fiber The amount of heat generated when the potting agent for the membrane module is cured increases, which may impair the filtration capacity of the hollow fiber membrane or the storage case of the hollow fiber membrane module. Furthermore, amine brushing is caused by the reaction of the amino group with carbon dioxide in the air, and the elution amount of the organic compound component from the potting agent for the hollow fiber membrane module may increase. On the other hand, when a bulky functional group such as an isopropyl group is bonded to the carbon to which the amino group is bonded, when the potting agent for the hollow fiber membrane module is cured, the amino group of the polyoxyalkylene diamine and the epoxy resin The reaction with the epoxy group does not proceed sufficiently, unreacted products are likely to remain, and the amount of the organic compound component eluted from the potting agent for the hollow fiber membrane module may increase.

  A commercial item can be used for the compound represented by Formula (3). The compound represented by the formula (3) is commercially available, for example, from Huntsuman under the trade names “Jeffamine D-230” and “Jeffamine D-400”.

  The curing agent contains at least one amine compound selected from the group consisting of polyoxyalkylene triamines and polyoxyalkylene diamines. The average functional number of the whole amine compound is 2.6 to 3.0, preferably 2.7 to 3.0, more preferably 2.8 to 3.0, and particularly preferably 2.9 to 3.0. preferable. When the average functional number of the amine compound is 2.6 to 3.0, the hollow fiber membrane module can be obtained without reducing the amount of heat generated when the potting agent for the hollow fiber membrane module is cured and without impairing the filtration performance of the hollow fiber membrane. While being able to manufacture easily, the elution amount of the organic compound component from the potting agent for hollow fiber membrane modules can be reduced by fully crosslinking and curing the potting agent for hollow fiber membrane modules.

  In addition, in this invention, the average functional number of an amine compound says the value calculated in the following way. The content of each polyoxyalkylene triamine contained in the amine compound is WTi, the molecular weight is MTi, the content of each polyoxyalkylene diamine contained in the amine compound is WDi, and the molecular weight is MDi. Is calculated based on the following equation. The amine compound contains k types of polyoxyalkylene triamines and p types of polyoxyalkylene diamines.

  The total amine value of the whole amine compound is 56 to 393, preferably 168 to 393, and more preferably 337 to 393. When the total amine value of the whole amine compound is 56 or more, the potting agent for the hollow fiber membrane module is cured to a sufficient crosslinking density, and elution of organic compound components from the potting agent for the hollow fiber membrane module can be reduced. The hollow fiber membrane module potting agent has an appropriate viscosity, and the hollow fiber membrane module potting agent is sufficiently infiltrated between the hollow fiber membranes, and the hollow fiber membranes, the hollow fiber membrane bundle and the storage case. Can be firmly integrated. When the total amine value of the whole amine compound is 393 or less, the amount of heat generated when the potting agent for the hollow fiber membrane module is cured is suppressed, and the hollow fiber membrane is filtered without impairing the filtration capacity of the hollow fiber membrane or the housing case of the hollow fiber membrane module. A yarn membrane module can be manufactured.

  The “total amine value” of the amine compound represents the number of mg of potassium hydroxide equivalent to perchloric acid equivalent to the total basic nitrogen contained in 1 g of a sample, and is an anonymous number. . In the present invention, the total amine value of an amine compound refers to a value measured according to JIS K7237.

  The content of the amine compound in the potting agent for the hollow fiber membrane module is 25 to 65 parts by weight with respect to 100 parts by weight of the epoxy resin, preferably 27 to 50 parts by weight, and more preferably 30 to 46 parts by weight. By setting the content of the amine compound in the potting agent for the hollow fiber membrane module within the above range, the amount of heat generated during curing of the potting agent for the hollow fiber membrane module is suppressed, and the hollow fiber membrane module is hollow without impairing the filtration performance of the hollow fiber membrane module. The point that the membrane module can be easily manufactured and the amount of elution of the organic compound component from the potting agent for the hollow fiber membrane module can be reduced by sufficiently crosslinking and curing the potting agent for the hollow fiber membrane module. It is possible to balance the points that can be done in a well-balanced manner.

  The above-mentioned amine compound is contained as a curing agent in the potting agent for the hollow fiber membrane module, but other curing agents may be contained within a range that does not impair the effects of the present invention. Examples of such curing agents include thiol compounds, dicyandiamides, imidazoles, aromatic polyamines, aliphatic polyamines, polyamides, polysulfides, dihydrazides, and the like.

  The potting agent for the hollow fiber membrane module may contain a curing catalyst as long as the effects of the present invention are not impaired. Such a curing catalyst is not particularly limited, and examples thereof include trimethylamine, triethylamine, tetraethylmethylenediamine, tetramethylpropane-1,3-diamine, tetramethylarehexane-1,6-diamine, pentamethyldiethylenetriamine, and pentamethyl. Dipropylene triamine, bis (2-dimethylaminoethyl) ether, ethylene glycol (3-dimethyl) aminopropyl ether, dimethylaminoethanol, dimethylaminoethoxyethanol, N, N, N′-trimethylaminoethylethanolamine, dimethylcyclohexylamine N, N-dimethylaminomethylphenol, N, N-dimethylpropialeamine, N, N, N ′, N′-tetramethylhexamethylenediamine, N, N, N ′, N ″, '' -Pentamethyldiethylenetriamine, N-methylpiperidine, N, N'-dimethylpiperazine, N, N-dimethylbenzylamine, dimethylaminomethylphenol, 2,4,6-tris (dimethylaminomethyl) phenol, 1,8 -Diazabicyclo [5.4.0] undecene-7,1,5-diazabicyclo [4.3.0] -nonene-5,6-dibutylamino-1,8-diazabicyclo [5.4.0] -undecene- 7,1,2-dimethylimidazole, dimethylpiperazine, N-methyl-N ′-(2-dimethylamino) -ethylpiperazine, N-methylmorpholine, N- (N ′, N′-dimethylamino) ethyl) morpholine, N-methyl-N ′-(2-hydroxyethyl) morpholine, triethylenediamine, hexamethylenete Lamin, etc. triethanolamine. In addition, a curing catalyst may be used independently or 2 or more types may be used together.

  As the curing catalyst, triethanolamine is preferable because the reaction rate can be easily controlled. As the curing catalyst, 2,4,6-tris (dimethylaminomethyl) phenol is preferable because the degree of curing of the cured product of the potting agent for the hollow fiber membrane module can be improved. By using triethanolamine and 2,4,6-tris (dimethylaminomethyl) phenol as the curing catalyst, the reaction rate is controlled and the degree of curing of the cured product of the potting agent for the hollow fiber membrane module is improved. be able to.

  The potting agent may contain an additive as long as the effects of the present invention are not impaired. Examples of the additive include thermoplastic resins, deodorizers, silane coupling agents, adhesion improvers such as titanium coupling agents / adhesion improvers, hindered amines, hydroquinones, antioxidants such as hindered phenols, UV absorbers such as benzophenones, benzotriazoles, salicylic acid esters, metal complex salts, metal soaps, stabilizers such as inorganic salts and organic salts of heavy metals (such as zinc, tin, lead, cadmium, etc.) and organic tin compounds Phthalates, phosphate esters, fatty acid esters, castor oil, liquid paraffin alkyl polycyclic aromatic hydrocarbons and other plasticizers, paraffin wax, microcrystalline wax, polymer wax, beeswax, whale wax, low molecular weight polyolefin, etc. Waxes, benzyl alcohol, tar, picchu Non-reactive diluents such as men, calcium carbonate, kaolin, talc, mica, bentonite, clay, sericite, glass fiber, carbon fiber, aramid fiber, nylon fiber, acrylic fiber, glass powder, glass balloon, shirasu balloon, coal Powder, acrylic resin powder, phenol resin powder, metal powder, ceramic powder, zeolite, slate powder and other fillers, carbon blanks, titanium oxide, red iron oxide, para red, bitumen and other pigments or dyes, ethyl acetate, toluene, alcohol , Ethers, ketones and other solvents, foaming agents, monoisocyanate compounds, carbodiimide compounds and other dehydrating agents, antistatic agents, antibacterial agents, fungicides, viscosity modifiers, fragrances, flame retardants, leveling agents, dispersants , Thixotropic imparting agents, conductivity imparting agents and the like.

  The potting agent for the hollow fiber membrane module is composed of two liquids, a main agent and a curing agent. The main component of the potting agent for the hollow fiber membrane module is, for example, a composition containing an epoxy resin and a reactive diluent using a general-purpose mixer. It can be manufactured by mixing. The curing agent for the hollow fiber membrane module potting agent is, for example, a polyoxyalkylene triamine, a curing catalyst added as necessary, and / or other curing agents, and a general-purpose mixer as required. It can manufacture by mixing using. Examples of the mixer include a mixer, an impeller type mixing stirrer, a dynamic mixer, a static mixer, and a kneader.

  An example of how to use the potting agent for the hollow fiber membrane module of the present invention will be described. First, the main component of the potting agent for the hollow fiber membrane module and the curing agent are uniformly mixed. The difference in viscosity between the main agent and the curing agent of the hollow fiber membrane module potting agent is small, and the main agent and the curing agent can be mixed uniformly. Next, a plurality of hollow fiber membranes formed in a thread shape are bundled in an aligned state. A pair of cylindrical storage cases are prepared, and caps are attached and closed at one end openings of the storage cases, and then both ends of the hollow fiber membrane bundle are stored in the storage cases. Subsequently, the potting agent for the hollow fiber membrane module is supplied into each storage case. The hollow fiber membrane allows the liquid to be filtered by permeating the liquid from the surface or the hollow part formed at the center of the hollow fiber membrane, and the filtered liquid can be taken out from the hollow part or the surface of the hollow fiber membrane. It is also called a hollow fiber.

  A state in which the hollow fiber membrane bundle is stored in the storage case by curing the potting agent for the hollow fiber membrane module at room temperature in a state where the end of the hollow fiber membrane bundle is immersed in the potting agent for the hollow fiber membrane module before curing. Then, the cap is removed from the storage case, and the hollow fiber membrane module can be manufactured by cutting off both ends of the hollow fiber membrane bundle. The potting agent for a hollow fiber membrane module can be cured at a low temperature, and can be cured without impairing the filtration ability of the hollow fiber membrane and the constituent members of the hollow fiber membrane module. The curing temperature of the potting agent for the hollow fiber membrane module is preferably 15 to 40 ° C, more preferably 20 to 30 ° C, particularly preferably 22 to 28 ° C, and most preferably 23 to 25 ° C.

  The potting agent for a hollow fiber membrane module is cured at a low temperature and has a low calorific value, and does not damage the components of the hollow fiber membrane and the hollow fiber membrane module. Less elution of organic compound components.

  Accordingly, the liquid filtered using the hollow fiber membrane module manufactured using the hollow fiber membrane module potting agent comes into contact with the cured product of the hollow fiber membrane module potting agent, but the hollow fiber membrane module potting agent. Since the amount of organic carbonized component elution from the cured product is kept low, the amount of organic compound component contained in the filtered liquid is reduced, and various uses such as beverage use and industrial use Can be used.

  The potting agent for a hollow fiber membrane module of the present invention is cured at a low temperature and has a low calorific value, does not damage the hollow fiber membrane and the constituent members of the hollow fiber membrane module, and cures the potting agent for the hollow fiber membrane module. The elution amount of organic compound components from the product is also small.

  Hereinafter, embodiments of the present invention will be described in more detail with reference to examples. However, the present invention is not limited to these examples.

(Epoxy resin)
Epoxy resin 1 (bisphenol A type epoxy resin, trade name “jER828” manufactured by Mitsubishi Chemical Corporation, epoxy equivalent: 184-194, conditions at 23 ° C. and 0.10 MPa: liquid)
Epoxy resin 2 (Bisphenol F type epoxy resin, trade name “jER806” manufactured by Mitsubishi Chemical Corporation, epoxy equivalent: 160 to 170, conditions at 23 ° C. and 0.10 MPa: liquid)
Epoxy compound 3 (phenol novolac type epoxy resin, trade name “jER152” manufactured by Mitsubishi Chemical Corporation, epoxy equivalent: 160 to 170, conditions at 23 ° C. and 0.10 MPa: liquid)
Epoxy compound 4 (glycidyl ether of 1,6-hexanediol, manufactured by ADEKA, trade name “ADEKA GLYCIROL ED-503”, epoxy equivalent: 165, 23 ° C. and 0.10 MPa conditions: liquid)

(Reactive diluent)
Reactive diluent 1 (monoglycidyl ether having a structure represented by formula (1), R ¹ : carbon number dodecyl group or tridecyl group, trade name “Epotec RD-108” manufactured by ADITYA BIRLA)
Reactive diluent 2 (reaction product of cashew nut shell liquid and epichlorohydrin, trade name “NC-513” manufactured by CARDOLITE)
Reactive diluent 3 (4-tert-butylphenylglycidyl ether, trade name “Araldite DY-P” manufactured by HANTSMAN)
Reactive diluent 4 (epoxidized soybean oil, trade name “Adekaizer O-130P” manufactured by ADEKA)
Reactive diluent 5 (o-methylphenyl glycidyl ether, trade name “Epotec RD-105” manufactured by ADITYA BIRLA)
Reactive diluent 6 (poly (propylene glycol) diglycidyl ether, product name “ERISYS GE-24” manufactured by CVC)
Reactive diluent 7 (epoxidized castor oil, trade name “ERISYS GE-35” manufactured by CVC)
Reactive diluent 8 (dimer acid epoxy resin, product name “ERISYS GS-120” manufactured by CVC)

(Amine compound)
Amine compound 1 (polyoxypropylene triamine, manufactured by Huntsman, trade name “Jeffamine T-403”, in formula (2), R ² , R ³ , R ⁴ and R ⁵ are methyl groups, X, Y and Z are positive (X + Y + Z) is 5-6; molecular weight: 440, total amine number: 342-387)
Amine compound 2 (polyoxypropylene triamine, trade name “XTJ-566” manufactured by Huntsman, in formula (2), R ² , R ³ and R ⁴ are ethyl groups, R ⁵ is a methyl group, X, Y and Z Is a positive number, (X + Y + Z) is 5-6; molecular weight: 400, total amine number: 370-387)
Amine compound 3 (polyoxypropylene diamine, manufactured by Huntsman, trade name “Jeffamine D-230”, in formula (3), R ⁶ and R ⁷ are methyl groups and n is 2.5; molecular weight: 230, amino group Having a methyl group on the carbon next to the total amine number: 454 to 488)
-Amine compound 4 (polyoxyethylenediamine, product name “Ancamine 1922A” manufactured by Air Products Japan, molecular weight: 220, no carbon atom next to the amino group, total amine number: 494 to 527)
Amine compound 5 (polyoxypropylene triamine, trade name “Jeffamine T-3000” manufactured by Huntsman, molecular weight: 3000, having a methyl group on the carbon next to the amino group, total amine value: 50 to 55)
Amine compound 6 (polyoxypropylene diamine, manufactured by Huntsman, trade name “Jeffamine D-400”, in formula (3), R ⁶ and R ⁷ are methyl groups and n is 6.1, molecular weight: 430, all amines Price: 230-263)

(Curing catalyst)
・ Curing catalyst 1 (Triethanolamine)
Curing catalyst 2 (2,4,6-tris (dimethylaminomethyl) phenol)
Curing catalyst 3 (N, N, N ′, N ″, N ″ -pentamethyldiethylenetriamine)

(Examples 1-20, Comparative Examples 1-14)
A composition containing predetermined amounts of epoxy resins 1 to 4 and reactive diluents 1 to 8 shown in Tables 1 to 3 was supplied to an impeller type mixing stirrer and uniformly mixed to prepare a main agent. A composition containing amine compounds 1 to 6 and curing catalysts 1 to 3 in predetermined amounts shown in Tables 1 to 3 was supplied to an impeller-type mixing stirrer and uniformly mixed to prepare a curing agent. A two-pack type potting agent for a hollow fiber membrane module containing a main agent and a curing agent was produced. In addition, although Example 10 of Table 1 and Table 2 is the same Example, it overlapped and described for convenience.

  In Example 15, the total amine value of the entire amine compound was 390. In Example 16, the total amine value of the entire amine compound was 328. In Comparative Example 13, the total amine value of the entire amine compound was 404. In Comparative Example 14, the total amine value of the entire amine compound was 307.

  About the obtained potting agent for hollow fiber membrane modules, the elution amount of the organic compound component, the reaction heat generation during curing, and the viscosity difference between the main agent and the curing agent were measured in the following manner, and the results are shown in Tables 1 to 3 Indicated. About the potting agent for hollow fiber membrane modules of Example 2 and 17-19, hardening time and hardening hardness were measured in the following way, and the result was shown in Table 2.

(Organic compound component)
After uniformly mixing the main component of the potting agent for the hollow fiber membrane module and the curing agent, the potting agent for the hollow fiber membrane module is poured into a flat plate mold having a thickness of 2 mm, and the potting agent for the hollow fiber membrane module is placed at 60 ° C. And cured for 48 hours to prepare a cured product.

  The obtained cured product was punched into a flat rectangular dumbbell having a length of 75 × width of 15 mm to prepare eight test pieces. Eight test pieces were placed in an Erlenmeyer flask washed by a method according to JIS S3200-7 so as not to overlap each other. Distilled water in the Erlenmeyer flask was sealed with a glass stopper by sliding 200 ml of distilled water as an eluent into the Erlenmeyer flask and making the test piece completely immersed in distilled water. Was allowed to stand at 60 ° C. for 48 hours. Then, after cooling the distilled water in the Erlenmeyer flask to 23 ° C., the TOC value was measured using a TOC meter (trade name “Sievers 5310C” manufactured by GEAI) and evaluated based on the following criteria.

(Reaction exotherm and curing time during curing)
After uniformly mixing the potting agent for the hollow fiber membrane module and the curing agent, in a 23 ° C. atmosphere, pouring 900 g of the potting agent for the hollow fiber membrane module into a steel can having a diameter of 140 mm and a height of 160 mm. Put a thermocouple (K φ0.32, JIS C1602 compliant) in the center of the potting agent for hollow fiber membrane module and use a data logger (trade name “GL220” manufactured by Graphtec Co., Ltd.) for potting agent for hollow fiber membrane module The heat of reaction during curing was measured, and the maximum exothermic temperature was measured. The time from when the main component of the potting agent for the hollow fiber membrane module and the curing agent were uniformly mixed until the maximum exothermic temperature was reached was measured, and was defined as the curing time.

(Difference in viscosity between main agent and curing agent)
The viscosities of the main component and the curing agent of the potting agent for hollow fiber membrane module were respectively No. 23 ° C. in accordance with JIS K7233. When the viscosity is less than 10000 mPa · s using a H rotor of No. 3, it is measured using a B-type viscometer under the condition of a rotation speed of 10 rpm and 10000 mPa · s or more at 5 rpm. The difference in viscosity was calculated and evaluated based on the following criteria.
Small: Less than 8000 mPa · s.
Large: 8000 mPa · s or more.

(Hardness)
The potting agent for the hollow fiber membrane module was cured in the same manner as the measurement procedure for the reaction exotherm during curing to prepare a cured product. The hardness of the cured product was measured using a type D durometer in an atmosphere of 30 ° C. according to JIS K6253. The measurement time was 10 seconds.

Claims (4)

100 parts by weight of an epoxy resin having an epoxy equivalent of 230 or less and an aromatic ring in the molecule and liquid at 23 ° C. and 0.10 MPa, and a reaction product of cashew nut shell liquid and epichlorohydrin, formula (1 A main agent containing 3 to 20 parts by weight of at least one reactive diluent selected from the group consisting of monoglycidyl ether having a structure represented by), 4-tert-butylphenyl glycidyl ether and epoxidized soybean oil; Contains 25 to 65 parts by weight of an amine compound containing at least one selected from the group consisting of oxyalkylene triamines and polyoxyalkylene diamines, having a total amine number of 56 to 393 and an average functionality of 2.6 to 3.0. A potting agent for a hollow fiber membrane module, comprising a curing agent.

In the formula (1), R ¹ is an alkyl group having 8 or more carbon atoms. The potting agent for a hollow fiber membrane module according to claim 1, wherein the amine compound is polyoxyalkylene triamine. The potting agent for a hollow fiber membrane module according to claim 1 or 2, wherein the epoxy resin is a bisphenol A type epoxy resin. The total amine value of an amine compound is 337-393, The potting agent for hollow fiber membrane modules of any one of Claims 1-3 characterized by the above-mentioned.