KR20160059908A - Drinking water parts comprsing polyketone polymer - Google Patents

Abstract

The present invention relates to a component for drinking water, which is produced by injection-molding a polyketone polymer and, more specifically, to a component for drinking water, which is produced by injection-molding a polyketone polymer, shows sufficient water resistance and impact strength by using polyketone which does not blend an anti-wear agent, and has the improved physical property maintenance rate.

Description

BACKGROUND OF THE INVENTION 1. Field of the Invention [0001] The present invention relates to a drinking water containing component including a polyketone polymer,

BACKGROUND OF THE INVENTION 1. Field of the Invention [0001] The present invention relates to a drink receiving part manufactured by injection molding a polyketone polymer, and more particularly to a drink receiving part having excellent abrasion resistance.

The development of industry and various harmful factors caused by environmental pollution are threatening human health. To this end, methods for reducing pollution due to various harmful substances and minimizing environmental pollution are proposed by using environmentally friendly and bio-materials.

For example, in general, plastic containers used for storing and storing drinking water and foodstuffs emit various harmful toxins, are not well maintained in the storage of drinking water, and do not decay after being disposed of, And so on.

As a typical plastic container, a PET bottle is produced by drying PET (Polytetheylene terephthalate) at high temperature to remove moisture from the PET, then dissolving the resin at a high temperature of 300 ° C. in an injection machine, Lt; / RTI > Thereafter, the preform is reheated and put into a mold of a desired shape, and air is injected to expand the preform.

PET bottles are extracted from petroleum and are made of polyethylene (PE, polyethylene) or polystyrene (PS, polystyrene), and the amount of petroleum is about 1/4 of PET bottle capacity.

Recently, PET bottles which do not use petroleum raw materials, for example, biodegradable polyester and corn raw materials, are being mixed to produce PET bottles, thereby promoting carbon reduction. However, it has an advantage in that it uses natural raw materials, but it has a limitation in that the amount of the material to be supplied is limited, and the production cost is relatively high compared to PET.

On the other hand, PET bottles based on petroleum raw materials are not easily retained in terms of storage of drinking water. Therefore, PET bottles are made by compressing other polymer layers, natural pulp, and aluminum foil to produce light, air, and moisture A method has been proposed.

However, since a similar process must be repeatedly performed, the production process is complicated and the production efficiency is relatively low as compared with the PET injection process, resulting in an increase in production costs.

On the other hand, polyketone (PK) is superior to general engineering plastic materials such as polyamide polyester and polycarbonate because of excellent heat resistance, chemical resistance, impact resistance and fuel permeability, and is widely applied to various industries.

The polyketone having the above characteristics can be produced by reacting carbon monoxide (CO) and an olefin such as ethylene or propylene as a catalyst with a transition metal complex such as palladium (Pd) or nickel (Ni) It is already known that carbon monoxide and olefin can be obtained by alternating bonding with each other by using a polymerization initiator (Industrial Materials, December issue, page 5, 1997).

In addition, the polyketone is included in general-purpose high-performance plastics and has an advantage in that it has high strength comparable to conventional engineering plastics and good affinity with rubber. Due to the characteristics of polyketone, polyketone can be used for tire cord or rubber material in which paraffin-based aramid fibers are exclusively used.

In order to solve the above problems, the inventors of the present invention have studied a polyketone resin, and as a result, they have been able to produce a polyketone resin composition having excellent impact resistance, scratch resistance and excellent physical property retention as compared with conventional engineering plastics.

Korean Patent No. 1006685720000 Korean Patent No. 1004453540000 Korean Patent No. 1008108650000

In order to solve the problems described above, it is an object of the present invention to provide a drinking-water receiving part which exhibits sufficient abrasion resistance and improved physical property retention by using a polyketone in which an anti-wear agent is not blended by injection molding using a polyketone polymer .

In order to achieve the above technical object, the present invention provides a process for producing a polyphenylene sulfide by injection-molding a linear alternating polyketone polymer composed of carbon monoxide and at least one olefinically unsaturated hydrocarbon and having a residual amount of palladium catalyst of 50 ppm or less and a molecular weight distribution of 1.5 to 2.5 Wherein the receiving portion is provided with a receiving portion.

The blend may further include 1 to 40% by weight of glass fibers.

The intrinsic viscosity of the linear alternating polyketone polymer is preferably 1.0 to 2.0 dl / g.

In addition, the above-mentioned drinking-water receiving part has an impact strength of 10 kJ / m 2 or more, a moisture absorption rate of less than 1.5% at 50 ° C and a relative humidity of 90% RH, an impact strength measured at 50 ° C and a relative humidity of 90% , And 85% or more of the impact strength measured at a relative humidity of 65% RH.

The drink receiving part according to the present invention can be manufactured by injection molding a polyketone polymer, thereby making it possible to manufacture a drink receiving part having improved impact strength and excellent water resistance and product moisture absorption rate.

Hereinafter, the present invention will be described in detail.

The present invention provides a drink receiving part which is made by injection molding a linear alternating polyketone polymer composed of carbon monoxide and at least one olefinically unsaturated hydrocarbon and having a residual amount of palladium catalyst of 50 ppm or less and a molecular weight distribution of 1.5 to 2.5.

Hereinafter, the polyketone polymer will be described as follows.

The polyketone polymer of the present invention is a linear alternating structure and substantially contains carbon monoxide per one molecule of unsaturated hydrocarbon. Ethylenically unsaturated hydrocarbons suitable for use as precursors of polyketone polymers have up to 20 carbon atoms, preferably up to 10 carbon atoms. Ethylenically unsaturated hydrocarbons can also be selected from the group consisting of ethene and alpha-olefins such as propene, 1-butene, iso-butene, 1- hexene, 1- octene, , Or an aryl aliphatic group containing an aryl substituent on another aliphatic molecule, particularly containing an aryl substituent on an ethylenically unsaturated carbon atom. Examples of aryl aliphatic hydrocarbons in ethylenically unsaturated hydrocarbons include styrene, p-methyl styrene, p-ethyl styrene and m-isopropyl styrene. The polyketone polymer preferably used in the present invention is a copolymer of carbon monoxide and ethene or a second ethylenically unsaturated hydrocarbon having carbon monoxide, ethene and at least three carbon atoms, in particular alpha-olefins such as propene Is a terpolymer.

 When the polyketone terpolymer is used as the main polymer component of the blend of the present invention, there are at least two units containing an ethylene moiety in each unit containing the second hydrocarbon moiety in the terpolymer. It is preferable that the number of units containing the second hydrocarbon moiety is from 10 to 100.

Preferred polymeric rings of the polyketone polymers in the present invention can be represented by the following formula (1).

[Chemical Formula 1]

- [CO- (-CH2-CH2-)] x- [CO- (G)] y-

In the above formula (1), G is an ethylenically unsaturated hydrocarbon, particularly an ethylenically unsaturated hydrocarbon having at least three carbon atoms, and x: y is preferably at least 1: 0.01.

In another embodiment, the polyketone polymer is a copolymer comprising repeating units represented by the general formulas (1) and (2), and y / x is preferably 0.03 to 0.3. When the value of the y / x value is less than 0.03, there is a limit in that the meltability and processability are inferior. When the value of y / x is more than 0.3, the mechanical properties are poor. Further, y / x is more preferably 0.03 to 0.1.

- [- CH2CH2-CO] x- (1)

- [- CH2 --CH (CH3) - CO] y - (2)

In addition, the melting point of the polymer can be controlled by controlling the ratio of ethylene to propylene in the polyketone polymer. For example, when the molar ratio of ethylene: propylene: carbon monoxide is adjusted to 46: 4: 50, the melting point is about 220 ° C, while the melting point is adjusted to 235 ° C when the molar ratio is adjusted to 47.3: 2.7: 50.

Particularly preferred are polyketone polymers having a number average molecular weight of from 100 to 200,000, especially from 20,000 to 90,000, as measured by gel permeation chromatography. The physical properties of the polymer are determined according to the molecular weight, depending on whether the polymer is a copolymer or a terpolymer and, in the case of a terpolymer, the properties of the second hydrocarbon part. The melting point of the total of the polymers used in the present invention is 175 ° C to 300 ° C, and generally 210 ° C to 270 ° C. The intrinsic viscosity (LVN) of the polymer measured by HFIP (hexafluoroisopropyl alcohol) at 60 DEG C using a standard tubular viscosity measuring apparatus is 0.5 dl / g to 10 dl / g, preferably 0.8 dl / g to 4 dl / g, And more preferably 1.0 dl / g to 2.0 dl / g. If the intrinsic viscosity is less than 0.5 dl / g, the mechanical properties are deteriorated. If the intrinsic viscosity exceeds 10 dl / g, the workability is deteriorated.

On the other hand, the molecular weight distribution of the polyketone is preferably 1.5 to 2.5, more preferably 1.8 to 2.2. When the ratio is less than 1.5, the polymerization yield decreases. When the ratio is 2.5 or more, the moldability is poor. In order to control the molecular weight distribution, it is possible to adjust proportionally according to the amount of the palladium catalyst and the polymerization temperature. That is, when the amount of the palladium catalyst is increased or when the polymerization temperature is 100 ° C or higher, the molecular weight distribution becomes larger.

As a method of producing the polyketone polymer, liquid phase polymerization in which carbon monoxide and olefin are carried out in an alcohol solvent through a catalyst composition composed of a palladium compound, an acid having 6 or less of PKa, and a ligand compound of phosphorus can be employed. The polymerization temperature is preferably from 50 to 100 ° C. and the reaction pressure is from 40 to 60 bar. The polymer is recovered through filtration and purification processes after polymerization, and the remaining catalyst composition is removed with a solvent such as alcohol or acetone.

This is preferred as palladium acetate and a palladium compound in the amount of 10 ^-3 to ^10-2 1mole preferred. Specific examples of the acid having a pKa value of 6 or less include trifluoroacetic acid, p-toluenesulfonic acid, sulfuric acid, and sulfonic acid. In the present invention, trifluoroacetic acid is used and its amount is preferably 6 to 20 equivalents based on palladium. Also, 1,3-bis [di (2-methoxyphenylphosphino)] propane is preferably used as the left-handed compound of phosphorus, and the amount to be used is preferably 1 to 1.2 equivalents based on palladium.

Hereinafter, the polymerization process of the polyketone polymer will be described in detail.

The repeating unit derived from carbon monoxide, an ethylenically unsaturated compound and one or more olefinically unsaturated hydrocarbon compounds, three or more copolymers, especially repeating units derived from carbon monoxide, and ethylenically unsaturated compounds and repeating units derived from propylenically unsaturated compounds are substantially Are excellent in mechanical properties and thermal properties, excellent in processability, high in abrasion resistance, chemical resistance and gas barrier property, and are useful materials for various applications. It is considered that the high molecular weight product of the copolymerized polyketone having three or more members is more useful as an engineering plastic material having higher workability and thermal properties and having excellent economy. Particularly, it has high abrasion resistance and can be used in light gasoline tanks because of high gas barrier properties such as parts of gears of automobiles, high chemical resistance, and lining materials of chemical transport pipes. In the case of using an ultrahigh molecular weight polyketone having an intrinsic viscosity of 2 or more as the fiber, it is possible to conduct stretching at a high magnification and to have a high strength and a high modulus of elasticity oriented in the stretching direction as belts, reinforcements of rubber hoses, tire cords, And is suitable for use in building materials and industrial materials.

The production method of polyketone is carried out in the presence of an organometallic complex catalyst comprising (a) a Group 9, 10 or 11 transition metal compound, and (b) a ligand having an element of Group 15 elements, Wherein the carbon monoxide, ethylene and propylene are subjected to liquid phase polymerization in a mixed solvent of an alcohol (e.g., methanol) and water to produce a linear terpolymer, As the solvent, a mixture of 100 parts by weight of methanol and 2 to 10 parts by weight of water may be used. If the content of water in the mixed solvent is less than 2 parts by weight, a ketal may be formed to lower the heat stability in the process. If the amount is more than 10 parts by weight, the mechanical properties of the product may be deteriorated.

Wherein the catalyst comprises (a) a Group 9, 10 or 11 transition metal compound of the Periodic Table of the Elements (IUPAC Inorganic Chemical Nomenclature, 1989) and (b) a ligand having an element of Group 15 elements.

Examples of the Group 9 transition metal compound in the ninth, tenth, or eleventh group transition metal compound (a) include complexes of cobalt or ruthenium, carbonates, phosphates, carbamates, and sulfonates, Specific examples thereof include cobalt acetate, cobalt acetylacetate, ruthenium acetate, ruthenium trifluoroacetate, ruthenium acetylacetate, and ruthenium trifluoromethanesulfonate.

 Examples of the Group 10 transition metal compounds include complexes of nickel or palladium, carbonates, phosphates, carbamates, sulfonates and the like. Specific examples thereof include nickel acetate, nickel acetylacetate, palladium acetate, palladium trifluoroacetate , Palladium acetylacetate, palladium chloride, bis (N, N-diethylcarbamate) bis (diethylamine) palladium and palladium sulfate.

 Examples of the Group 11 transition metal compound include copper or silver complexes, carbonates, phosphates, carbamates, and sulfonates, and specific examples thereof include copper acetate, copper trifluoroacetate, copper acetylacetate, Examples of the fluoroacetic acid include silver acetyl acetate, trifluoromethanesulfonic acid and the like.

 Of these, the transition metal compound (a), which is preferable inexpensively and economically, is nickel and copper compounds, and the preferable transition metal compound (a) in terms of the yield of the polyketone and the molecular weight is the palladium compound, It is most preferable to use palladium acetate.

Examples of the ligands (b) having an atom of Group XIII include 2,2'-bipyridyl, 4,4'-dimethyl-2,2'-bipyridyl, 2,2'- Bis (diphenylphosphino) ethane, 1,3-bis (diphenylphosphino) propane, 1,4-bis (diphenylphosphino) (2-methoxyphenyl) propane, 1,3-bis [di (2-isopropyl) Bis (diphenylphosphino) cyclohexane, 1,2-bis (diphenylphosphino) phosphine] propane, (Diphenylphosphino) methyl] benzene, 1,2-bis [[di (2-methoxyphenyl) (Diphenylphosphino) ferrocene, 2-hydroxy-1,3-bis [di (2-methoxy- (2-methoxyphenyl) phosphino] propane, 2,2-dimethyl-1,3-bis [di (2- Spinosyns; there may be mentioned a ligand, such as propane.

Among these ligands, preferred ligands (b) having a Group 15 element are phosphorus ligands having an atom of Group 15, and particularly preferred ligands in terms of yield of polyketone are 1,3-bis [di (2- Methoxyphenyl) phosphino] propane and 1,2-bis [[di (2-methoxyphenyl) phosphino] methyl] benzene, Di (2-methoxyphenyl) phosphino] propane, and it is safe in that it does not require an organic solvent. Soluble sodium salts such as 1,3-bis [di (2-methoxy-4-sulfonic acid sodium-phenyl) phosphino] propane, 1,2- ] Methyl] benzene, and 1,3-bis (diphenylphosphino) propane and 1,4-bis (diphenylphosphino) butane are preferred for ease of synthesis and availability in large quantities and economically. The preferred ligand (b) having a Group 15 atom is 1,3-bis [di (2-methoxyphenyl) phosphino] propane or 1,3-bis (diphenylphosphino) Bis (di (2-methoxyphenyl) phosphino] propane or ((2,2-dimethyl-1,3-dioxane-5,5- -Methoxyphenyl) phosphine).

(2)

Bis (bis (2-methoxyphenyl) phosphine) bis ((2,2-dimethyl-1,3-dioxane-5,5- Activity equivalent to that of 3,3-bis- [bis- (2-methoxyphenyl) phosphanylmethyl] -1,5-dioxa-spiro [5,5] undecane, which is known to exhibit the highest activity among polymerization catalysts The structure is simpler and has a lower molecular weight. As a result, the present invention has been able to provide a novel polyketone polymerization catalyst having the highest activity as a polyketone polymerization catalyst of the present invention, while further reducing its manufacturing cost and cost. A method for producing a ligand for a polyketone polymerization catalyst is as follows. ((2,2-dimethyl) -2,3-dioxolane was obtained by using bis (2-methoxyphenyl) phosphine, 5,5-bis (bromomethyl) Bis (bis (methylene)) bis (bis (2-methoxyphenyl) phosphine) is obtained by reacting a bis (methylene) . The process for preparing a ligand for a polyketone polymerization catalyst according to the present invention is a process for producing a ligand for a polyketone polymerization catalyst which comprises reacting 3,3-bis- [bis- (2-methoxyphenyl) phosphanylmethyl] -1,5-dioxa-spiro [5,5] ((2,2-dimethyl-1,3-dioxane-5,5-diyl) bis (methylene)) bis (bis (2- Methoxyphenyl) phosphine) can be commercially synthesized in a large amount.

In a preferred embodiment, the process for preparing a ligand for a polyketone polymerization catalyst of the present invention comprises: (a) introducing bis (2-methoxyphenyl) phosphine and dimethylsulfoxide (DMSO) into a reaction vessel under nitrogen atmosphere, Adding sodium and stirring; (b) adding 5,5-bis (bromomethyl) -2,2-dimethyl-1,3-dioxane and dimethylsulfoxide to the resulting mixture, followed by stirring and reacting; (c) adding methanol and stirring after completion of the reaction; (d) adding toluene and water, separating the layers, washing the oil layer with water, drying with anhydrous sodium sulfate, filtering under reduced pressure, and concentrating under reduced pressure; And (e) the residue was recrystallized from methanol to obtain ((2,2-dimethyl-1,3-dioxane-5,5- diyl) bis (methylene)) bis (bis (2- methoxyphenyl) And a step of acquiring the image data.

The amount of the Group 9, Group 10 or Group 11 transition metal compound (a) to be used varies depending on the kinds of the ethylenic and propylenically unsaturated compounds to be selected and other polymerization conditions. Therefore, But it is usually from 0.01 to 100 mmol, preferably from 0.01 to 10 mmol, per 1 liter of the reaction zone. The capacity of the reaction zone means the liquid phase capacity of the reactor. The amount of the ligand (b) to be used is not particularly limited, but is usually 0.1 to 3 mol, preferably 1 to 3 mol, per 1 mol of the transition metal compound (a).

Further, the addition of benzophenone in the polymerization of the polyketone is another characteristic. In the present invention, an effect of improving the intrinsic viscosity of the polyketone can be achieved by adding benzophenone in the polymerization of the polyketone. The molar ratio of (a) the ninth, tenth or eleventh transition metal compound to benzophenone is 1: 5-100, preferably 1:40-60. If the molar ratio of the transition metal to the benzophenone is less than 1: 5, the effect of improving the intrinsic viscosity of the produced polyketone is unsatisfactory. If the molar ratio of the transition metal to the benzophenone exceeds 1: 100, It is not preferable because it tends to decrease

Examples of the ethylenically unsaturated compound copolymerized with carbon monoxide include ethylene, propylene, 1-butene, 1-hexene, 4-methyl-1-pentene, 1-octene, -Olefins such as hexadecene and vinylcyclohexane; Alkenyl aromatic compounds such as styrene and? -Methylstyrene; But are not limited to, cyclopentene, norbornene, 5-methylnorbornene, 5-phenylnorbornene, tetracyclododecene, tricyclododecene, tricyclodecene, pentacyclopentadecene, pentacyclohexadecene, Cyclic olefins such as cyclododecene; Vinyl halides such as vinyl chloride; Ethyl acrylate, and acrylates such as methyl acrylate. Of these, preferred ethylenically unsaturated compounds are? -Olefins, more preferably? -Olefins having 2 to 4 carbon atoms, and most preferably ethylene.

 Wherein the carbon monoxide and the ethylenically unsaturated compound and the propylenically unsaturated compound are copolymerized with an organometallic complex comprising a ligand (b) having an element of group 9, group 10 or group 11 transition metal compound (a) or group 15 Catalyzed, the catalyst is produced by contacting the two components. Any method may be employed as the method of contacting. That is, the solution may be prepared as a solution in which two components are premixed in a suitable solvent, or the two components may be supplied separately to the polymerization system and contacted in the polymerization system.

In the present invention, conventionally known additives such as an antioxidant, a stabilizer, a filler, a refractory material, a releasing agent, a coloring agent, and other materials may be further added to improve the processability and physical properties of the polymer.

 As the polymerization method, a solution polymerization method using a liquid medium, a suspension polymerization method, a vapor phase polymerization method in which a small amount of a polymer is impregnated with a high concentration catalyst solution, and the like are used. The polymerization may be either batchwise or continuous. The reactor used in the polymerization can be used as it is or in a known manner. The polymerization temperature is not particularly limited, and is generally 40 to 180 占 폚, preferably 50 to 120 占 폚. The pressure at the time of polymerization is not particularly limited, but is generally from normal pressure to 20 MPa, preferably from 4 to 15 MPa.

A linear alternating polyketone is formed by the polymerization method as described above.

On the other hand, the present invention can produce a blend comprising the polyketone polymer and the glass fiber.

The glass fiber is preferably 1 to 40% by weight based on 100% by weight of the total blend, but is not limited thereto.

Hereinafter, a manufacturing method for manufacturing the drinking water part of the present invention is as follows.

A method for producing a drinking water part according to the present invention comprises: preparing a catalyst composition comprising a palladium compound, an acid having a pKa value of 6 or less, and a bidentate compound of phosphorus; Preparing a mixed solvent (polymerization solvent) containing an alcohol (for example, methanol) and water; Conducting the polymerization in the presence of the catalyst composition and the mixed solvent to prepare a linear terpolymer of carbon monoxide, ethylene and propylene; Removing the remaining catalyst composition from the linear terpolymer with a solvent (e.g., alcohol and acetone) to obtain a polyketone polymer; And injection molding a blend comprising the polyketone polymer or the polyketone polymer and glass fibers.

As the palladium compound constituting the catalyst composition, palladium acetate can be used. The amount of the palladium compound to be used is preferably 10 ^-3 to 10 ^-1 mole, but is not limited thereto.

The acid having the pKa value of 6 or less constituting the catalyst composition may be at least one selected from the group consisting of trifluoroacetic acid, p-toluenesulfonic acid, sulfuric acid and sulfonic acid, preferably trifluoroacetic acid. The amount to be used is suitably 6 to 20 (mol) equivalents based on the palladium compound.

Examples of the bidentate ligand compound constituting the catalyst composition include 1,3-bis [diphenylphosphino] propane (for example, 1,3-bis [di (2-methoxyphenylphosphino)] propane, , 3-bis [bis [anilyl] phosphinomethyl] -1,5-dioxaspiro [5,5] undecane and ((2,2-dimethyl-1,3-dioxane- ) Bis (bis (methylene)) bis (bis (2-methoxyphenyl) phosphine), and the amount thereof is suitably 1 to 20 (mol) relative to the palladium compound.

The carbon monoxide, ethylene and propylene are liquid phase polymerized in a mixed solvent of alcohol (e.g. methanol) and water to produce a linear terpolymer. As the mixed solvent, a mixture of 100 parts by weight of methanol and 2 to 10 parts by weight of water may be used. If the content of water in the mixed solvent is less than 2 parts by weight, a ketal may be formed to lower the heat stability in the process. If the amount is more than 10 parts by weight, the mechanical properties of the product may be deteriorated.

The polymerization temperature is preferably in the range of 50 to 100 ° C and the reaction pressure in the range of 40 to 60 bar. The resulting polymer is recovered through filtration and purification processes after polymerization, and the remaining catalyst composition is removed with a solvent such as alcohol or acetone.

A polymer can be produced by the above-mentioned method and extruded or injection-molded to produce a drinking water part.

In this case, the extrusion temperature is preferably 230 to 260 ° C, and the screw rotation speed is preferably in the range of 100 to 300 rpm. If the extrusion temperature is less than 230 캜, kneading may not occur properly, and if the extrusion temperature exceeds 260 캜, problems related to the heat resistance of the resin may occur. If the screw rotational speed is less than 100 rpm, the kneading may not be smoothly performed, and if it exceeds 300 rpm, the mechanical properties may deteriorate.

The drinking water component according to the present invention has an impact strength of 10 kJ / m 2 or more, a moisture absorption rate of less than 1.5% at 50 캜 and a relative humidity of 90% RH, an impact strength measured at 50 캜 and a relative humidity of 90% , And 85% or more of the impact strength measured at a relative humidity of 65% RH.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in more detail with reference to specific embodiments. However, these embodiments are merely intended to clarify the present invention and are not intended to limit the scope of the present invention. The present invention will be described in detail with reference to the following non-limiting examples.

Example 1

The linear alternating polyketone terpolymer of carbon monoxide and ethylene and propene is prepared by reacting palladium acetate, trifluoroacetic acid and ((2,2-dimethyl-1,3-dioxane-5,5-diyl) bis (methylene) Bis (2-methoxyphenyl) phosphine). In the above, the content of trifluoroacetic acid with respect to palladium is 11 times the molar ratio, and the two stages of the first stage at a polymerization temperature of 80 ° C and the second stage at 84 ° C are carried out. The molar ratio of ethylene to propene in the polyketone terpolymer prepared above was 46 to 4. The melting point of the polyketone terpolymer is 220 DEG C, the LVN measured at 25 DEG C by HFIP (hexa-fluoroisopropano) is 1.2 dl / g, the MI index is 60 g / 10 min, the MWD is 2.0, The residual amount was 5 ppm. The polyketone terpolymer prepared above was molded into a pellet on an extruder using a twin screw having a diameter of 40 mm and L / D = 32, which was operated at 250 rpm, and then injection molded to prepare a specimen for drinking water components .

Example 2

The linear alternating polyketone terpolymer of carbon monoxide and ethylene and propene is prepared by reacting palladium acetate, trifluoroacetic acid and ((2,2-dimethyl-1,3-dioxane-5,5-diyl) bis (methylene) Bis (2-methoxyphenyl) phosphine). In the above, the content of trifluoroacetic acid with respect to palladium is 10 times the molar ratio, and the two stages of the first stage at a polymerization temperature of 78 占 폚 and 84 占 폚 are carried out. The molar ratio of ethylene to propene in the polyketone terpolymer prepared above was 46 to 4. The melting point of the polyketone terpolymer is 220 DEG C, the LVN measured at 25 DEG C by HFIP (hexa-fluoroisopropano) is 1.4 dl / g, the MI index is 60 g / 10 min, the MWD is 2.0, The residual amount was 3 ppm. The polyketone terpolymer prepared above was molded into pellets on an extruder using a twin screw having a diameter of 40 mm and L / D = 32 operating at 250 rpm and injection molded to prepare specimens for drinking water parts.

Example 3

The linear alternating polyketone terpolymer of carbon monoxide and ethylene and propene is prepared by reacting palladium acetate, trifluoroacetic acid and ((2,2-dimethyl-1,3-dioxane-5,5-diyl) bis (methylene) Bis (2-methoxyphenyl) phosphine). In the above, the content of trifluoroacetic acid with respect to palladium is 9 times the molar ratio, and the two stages of the first stage at a polymerization temperature of 74 deg. C and the second stage at 84 deg. The molar ratio of ethylene to propene in the polyketone terpolymer prepared above was 46 to 4. The melting point of the polyketone terpolymer is 220 DEG C, the LVN measured at 25 DEG C by HFIP (hexa-fluoroisopropano) is 1.6 dl / g, the MI index is 60 g / 10 min, the MWD is 2.0, The residual amount was 4 ppm. The polyketone terpolymer prepared above was molded into pellets on an extruder using a twin screw having a diameter of 40 mm and L / D = 32 operating at 250 rpm and injection molded to prepare specimens for drinking water parts.

Example 4

The linear alternating polyketone terpolymer of carbon monoxide and ethylene and propene is prepared by reacting palladium acetate, trifluoroacetic acid and ((2,2-dimethyl-1,3-dioxane-5,5-diyl) bis (methylene) Bis (2-methoxyphenyl) phosphine). In the above, the content of trifluoroacetic acid with respect to palladium is 10 times the molar ratio, and the two stages of the first stage at a polymerization temperature of 78 占 폚 and 84 占 폚 are carried out. The molar ratio of ethylene to propene in the polyketone terpolymer prepared above was 46 to 4. The melting point of the polyketone terpolymer is 220 DEG C, the LVN measured at 25 DEG C by HFIP (hexa-fluoroisopropanol) is 1.4 dl / g, the MI index is 60 g / 10 min, the MWD is 1.8, The residual amount was 5 ppm. The polyketone terpolymer prepared above was molded into pellets on an extruder using a twin screw having a diameter of 40 mm and L / D = 32 operating at 250 rpm and injection molded to prepare specimens for drinking water parts.

Example 5

The linear alternating polyketone terpolymer of carbon monoxide and ethylene and propene is prepared by reacting palladium acetate, trifluoroacetic acid and ((2,2-dimethyl-1,3-dioxane-5,5-diyl) bis (methylene) Bis (2-methoxyphenyl) phosphine). In the above, the content of trifluoroacetic acid with respect to palladium is 10 times the molar ratio, and the two stages of the first stage at a polymerization temperature of 78 占 폚 and 84 占 폚 are carried out. The molar ratio of ethylene to propene in the polyketone terpolymer prepared above was 46 to 4. The melting point of the polyketone terpolymer is 220 DEG C, the LVN measured at 25 DEG C by HFIP (hexa-fluoroisopropano) is 1.4 dl / g, the MI index is 60 g / 10 min, the MWD is 2.2, The residual amount was 6 ppm. The polyketone terpolymer prepared above was molded into pellets on an extruder using a twin screw having a diameter of 40 mm and L / D = 32 operating at 250 rpm and injection molded to prepare specimens for drinking water parts.

Example 6

The linear alternating polyketone terpolymer of carbon monoxide and ethylene and propene is prepared by reacting palladium acetate, trifluoroacetic acid and ((2,2-dimethyl-1,3-dioxane-5,5-diyl) bis (methylene) Bis (2-methoxyphenyl) phosphine). In the above, the content of trifluoroacetic acid with respect to palladium is 10 times the molar ratio, and the two stages of the first stage at a polymerization temperature of 78 占 폚 and 84 占 폚 are carried out. The molar ratio of ethylene to propene in the polyketone terpolymer prepared above was 46 to 4. The melting point of the polyketone terpolymer is 220 DEG C, the LVN measured at 25 DEG C by HFIP (hexa-fluoroisopropano) is 1.4 dl / g, the MI index is 60 g / 10 min, the MWD is 2.0, The residual amount was 7 ppm. A blend comprising 70 wt% of the polyketone terpolymer prepared above and 30 wt% of glass fiber was extruded onto a pellet on an extruder using a twin screw having a diameter of 40 mm and operating at 250 rpm and L / D = 32 Specimens of drinking water parts were manufactured by injection molding.

Comparative Example 1

A blend containing 70% by weight of nylon 6 and 30% by weight of glass fibers was made into a pellet on an extruder using a twin screw having a diameter of 40 cm and operating at 250 rpm and L / D = 32, The specimens of drinking water parts were manufactured by molding.

Property evaluation

The properties of the specimens prepared in Examples 1 to 6 and Comparative Example 1 were evaluated by the following methods. The results are shown in Table 1 below.

1. Impact strength: ASTM D256.

2. Evaluation of water resistance property retention: The specimens were treated under standard conditions (25 ℃, 65% RH relative humidity, 24 hours) and high temperature and high humidity conditions (50 ℃, 90% RH, 24 hours), according to ASTM D256 , And the average value of the measured values in five vertical and horizontal directions was taken for each treatment sample.

3. Evaluation of Product Moisture Content: Moisture content was measured after treatment for 24 hours at a temperature of 50 ° C and a relative humidity of 90%.

Example 1 Example 2 Example 3 Example 4 Example 5 Example 6 Comparative Example 1 Properties IV: 1.2
MWD: 2.0 IV: 1.4
MWD: 2.0 IV: 1.6
MWD: 2.0 IV: 1.4
MWD: 1.8 IV: 1.4
MWD: 2.2 POK + GF NY6 + GF Impact strength
(kJ / m2) 11 14 17 15 15 15 5 Product water resistance
(%, Property retention rate) 85 86 87 89 90 90 52 Product moisture absorption rate
(%, 50 ° C, 90% RH) 1.0 0.9 1.1 1.2 1.3 1.2 3.0

As can be seen from Table 1, the water resistance and impact strength of the examples were improved compared to the comparative examples. Particularly, in the case of the embodiment of the present invention, when the impact strength is 10 kJ / m 2 or more and the moisture absorption rate is less than 1.5% at 50 캜 and 90% RH and the impact strength measured at 50 캜 and 90% RH is 25 ℃, and relative humidity of 65% RH.

Claims (5)

Characterized in that it is produced by injection molding a blend comprising carbon monoxide and at least one olefinically unsaturated hydrocarbon, wherein the balance comprises a linear alternating polyketone polymer having a residual amount of palladium catalyst of 50 ppm or less and a molecular weight distribution of 1.5 to 2.5. part.
The method according to claim 1,
Wherein the blend further comprises 1 to 40% by weight of glass fibers.
The method according to claim 1,
The ligand of the catalyst composition in the polymerization of the linear alternating polyketone may be selected from the group consisting of bis (2,2-dimethyl-1,3-dioxane-5,5-diyl) bis (methylene) Pin).
The method according to claim 1,
Wherein said linear alternating polyketone polymer has an intrinsic viscosity of 1.0 to 2.0 dl / g.
The method according to claim 1,
Wherein the water-absorbing component has an impact strength of 10 kJ / m 2 or more, a moisture absorption rate of less than 1.5% at 50 캜 and a relative humidity of 90% RH, an impact strength measured at 50 캜 and a relative humidity of 90% And a level of 85% or more of the impact strength measured at a humidity of 65% RH.