CN102888111A - Preparing method of polyphenylene sulfide ceramic alloy - Google Patents

Preparing method of polyphenylene sulfide ceramic alloy Download PDF

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CN102888111A
CN102888111A CN2011101998505A CN201110199850A CN102888111A CN 102888111 A CN102888111 A CN 102888111A CN 2011101998505 A CN2011101998505 A CN 2011101998505A CN 201110199850 A CN201110199850 A CN 201110199850A CN 102888111 A CN102888111 A CN 102888111A
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polyphenylene sulfide
oxidation
screw extruder
glass fibre
polymethylmethacrylate
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CN102888111B (en
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刘彬
苟梁武
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SICHUAN DEYANG SPECIAL NEW MATERIALS CO Ltd
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Abstract

The invention discloses a preparing method of polyphenylene sulfide ceramic alloy The method comprises adding an anti-oxidant, elastomer powder of poly(methyl methacrylate), alumina ceramic powder with nanoscale of 95% and other fillers into the crosslinked polyphenylene sulfide, fully and uniformly mixing in a high-speed mixer to obtain a premix of the polyphenylene sulfide, inputting the premix of the polyphenylene sulfide and the fiberglass treated by a surface treatment agent of beta-(3,4-epoxy cyclohexyl)ethyltrimethoxysilane into a double-screw extruder for mixing, extruding and molding, and then cooling and cutting to form the finished composite granulates. The composite granulates obtained by the method has advantages of high thermal denaturation stability and tensile strength, and low metal corrosion, and can be widely applied in the fields of electronic appliances, machinery, chemical industry, petroleum, military industry, and aerospace.

Description

A kind of manufacture method of polyphenylene sulfide ceramal
Affiliated technical field
The invention belongs to speciality polymer material Application Areas
Background technology
Polyphenylene sulfide (PPS) good heat stability, has outstanding high thermal resistance, fusing point reaches 285 ℃, other special engineering plastics that are higher than present suitability for industrialized production, the PPS composite granule has good injection processing characteristics, can be processed into the PPS composite product of all size, different shape.But in the more harsh field of some application conditions, explore and find that the more good PPS matrix material of performance is still the target that people pursue.
Introduced among the Chinese patent CN:1667044A and a kind ofly added aromatic phosphoric ester and polyphenylene oxides is the manufacture method of the polyphenyl thioether composite material of resin, its objective is at injection molding SHI and improve the heat-resistant stability of matrix material and the surface smoothness of shaped material.But the dispersion effect of aromatic phosphoric ester in polyphenylene sulfide is undesirable, easily forms the parcel phenomenon when producing under the general technology level, thereby directly have influence on high-temperature mechanical property in pellet.
Introduced among the Chinese patent CN:1253149A and a kind ofly added epoxy silane compounds and high component is inorganic, the manufacture method of the polyphenylene sulfide of organic fibre (PPS) matrix material, its objective is and want to reduce this matrix material at the overlap of injection molded.Thereby provide a kind of have good processing characteristics, the polyphenyl thioether composite material of physical strength, although the overlap behind the packing materials such as adding epoxy silane compounds when being injected into part reduces, and has but reduced resistance to impact shock and the tensile strength of polyphenyl thioether composite material.
Introduced the manufacture method that employing zinc oxide palpus crystalline substance and glass fibre or carbon fiber and polyphenylene sulfide (PPS) resin carry out polyphenylene sulfide (PPS) matrix material of blending and modifying among the Chinese patent CN:1272124A, its objective is that adopting zinc oxide is that corrosion inhibitor improves corrosion of metal, can eliminate the detrimentally affect of mechanical-physical character; But after adding zinc oxide, tensile strength and the elongation at break of the polyphenylene sulfide of making (PPS) matrix material injection forming decrease, and its resistance to impact shock also decreases.
Introduced a kind of production method that adds the polyphenylene sulfide ceramal of thermo-stabilizer and mineral filler in Chinese patent application number NO:200710049503.8, this patent is to adopt very common method poly-p-phenylene sulfide ether resin to carry out modification to strengthen in fact.
In view of the above shortcoming of prior art, the objective of the invention is to study a kind ofly produce shock-resistant, high stabile against thermal denaturation, tensile strength is good and the polyphenylene sulfide ceramal matrix material that contains glass fibre low to metallic corrosion, good processability.
Summary of the invention:
Its main technique comprises:
A kind of manufacture method of polyphenylene sulfide ceramal, polyphenylene sulfide Preblend behind adding oxidation inhibitor, the ceramic powder is fully mixed in homogenizer, be shaped, form composite granule through cooling, pelletizing with glass fibre input parallel dual-screw extruding machine mixing extrusion again, it is characterized in that, adopt following processing step:
1), be 3-5 ten thousand with weight-average molecular weight, melt flow index is that 300-600g/10min and molecular weight distribution are the linear polyphenylene sulfide resin of 2.5-3.0, adds the crosslinked 2-3h of the heat of oxidation in the crosslinked device of the heat of oxidation;
2), will be 1) in homogenizer, fully mix after adding the weighting agents such as antioxidant, polymethylmethacrylate elastomerics in the polyphenylene sulfide cross-linked resin that obtains, the weight ratio of used antioxidant phosphorous acid triphenylmethyl methacrylate in the ninth of the ten Heavenly Stems and polyphenylene sulfide is 3-3.5: 100; The weight ratio of polymethylmethacrylate elastomerics and polyphenylene sulfide is 3-5: 100, and granularity is that the nano level 95% alumina-ceramic powder of 5-10nm and the weight ratio of polyphenylene sulfide are 30-40: 100 obtain polyphenylene sulfide Preblend with this;
3), with (2) gained polyphenylene sulfide Preblend 60-70%wt again with through β-(3, the 4-epoxycyclohexyl) the 40-30%wt diameter was the glass fibre input twin screw extruder of 20-30um after ethyl trimethoxy silane (A-168) surface treatment agent was processed, and formed the finished product composite granule through the shaping of twin screw extruder mixing extrusion, cooling, pelletizing.
4), in polyphenylene sulfide Preblend manufacturing processed, need to add the polymethylmethacrylate elastomerics, the overlap length of moulding is 0.3-0.5um, improve simultaneously the toughness of 30-40% polyphenyl thioether composite material, and the melt strength of polyphenyl thioether composite material improves 15-20%.
Melt strength refers to that polymkeric substance supports the ability of sole mass under molten state. macromolecule melt intensity (Melt Strength), sometimes be also referred to as melt elasticity (Melt Elasticity), approximately measuring polymer melting elongational viscosity (Elongational Viscosity) on the engineering, itself and molecular weight of polymers (MW), molecular weight distribution (MWD), branch chain (Branching) what/length etc. is relevant.Be exactly the degree of entanglement (Degree of Polymer Chain Entanglement at MelT) that depends under the polymer molten state in fact in the final analysis, degree of entanglement is high, and melt strength is just high.So can improve macromolecule melt intensity by branch chain or crosslinked (Cross-linking).
In general, the product that melt strength is high relatively is fit to extrude, and the product that melt strength is low relatively is fit to injection moulding; It is rightabout that melt strength and molten finger numerically are into, that is to say that melt strength is higher, and molten finger is lower.But whether be fit to extrude or injection moulding less than obviously distinguishing, relevant with processing condition.Also have, the melt strength of injection moulding is embodied under the high-shear, therefore still should be noted that here.Melt strength is not only relevant with molecular weight, and the quantity of the side chain in the molecule and length relation are very large.
In the manufacture method of the polyphenylene sulfide alloy that contains the porcelain powder of the present invention, the melt strength of matrix material is not measure under the condition that strengthens with fortifying fibre.
The composite granule that adopts as above method to make has high stabile against thermal denaturation and tensile strength, and is low to the metallic corrosion rate.Can be widely used in electronic apparatus, machinery, chemical industry, oil, military project, field of aerospace.
Adding the elastomeric purpose of polymethylmethacrylate in the process of the present invention is the burr (overlap) that reduces on the one hand moulding, improve on the other hand the melt strength of matrix material in injection moulding process, the 3rd, reduce the degree of crystallinity of matrix material and the crystallization velocity of raising matrix material, can reduce so the various losses of matrix material in injection moulding process, improve the yield rate of moulding.
In homogenizer, stir 2-3h after adding polyphenylene sulfide cross-linked resin, oxidation inhibitor, polymethylmethacrylate elastomerics, ceramics powder, make it be mixed into homogeneous polyphenylene sulfide mixture, then with process β-(3, the 4-epoxycyclohexyl) single fiber diameter was the glass fibre input twin screw extruder of 20-30um after ethyl trimethoxy silane (A-168) surface treatment agent was processed, form the finished product composite granule through the shaping of twin screw extruder mixing extrusion, cooling, pelletizing, pack at last, put in storage, use.
The inventive method gained composite granule has high stabile against thermal denaturation and tensile strength, and is low to the metallic corrosion rate.Can be widely used in electronic apparatus, machinery, chemical industry, oil, military project, field of aerospace.
Description of drawings:
Fig. 1 is process flow sheet of the present invention.
Fig. 2 is the product performance table that embodiment of the invention experiment obtains.
Embodiment
Embodiment 1
Be 30,000 with weight-average molecular weight, melt flow index is that 600g/10min and molecular weight distribution are 3.0 linear polyphenylene sulfide resin, adds in the crosslinked device of the heat of oxidation the crosslinked 3h of the heat of oxidation stand-by
In homogenizer, add 64%wt polyphenylene sulfide cross-linked resin, 3%wt phosphorous acid triphenylmethyl methacrylate in ninth of the ten Heavenly Stems oxidation inhibitor, 3%wt polymethylmethacrylate elastomerics, the 30%wt granularity is to stir 3h behind the nano level 95% alumina-ceramic powder of 5nm, make it be mixed into homogeneous polyphenylene sulfide mixture, then the Preblend of 60%wt polyphenylene sulfide and 40%wt are through β-(3, the 4-epoxycyclohexyl) single fiber diameter was the glass fibre input twin screw extruder of 30um after ethyl trimethoxy silane (A-168) surface treatment agent was processed, be shaped through the twin screw extruder mixing extrusion, cooling, pelletizing forms the finished product composite granule, at last packing, warehouse-in, use.
The various physicalies of the polyphenyl thioether composite material that obtains with aforesaid method will show in Table 1.
Embodiment 2
Be 50,000 with weight-average molecular weight, melt flow index is that 300g/10min and molecular weight distribution are 2.5 linear polyphenylene sulfide resin, adds in the crosslinked device of the heat of oxidation the crosslinked 2h of the heat of oxidation stand-by
In homogenizer, add 51.5%wt polyphenylene sulfide cross-linked resin, 3.5%wt phosphorous acid triphenylmethyl methacrylate in ninth of the ten Heavenly Stems oxidation inhibitor, 5%wt polymethylmethacrylate elastomerics, the 40%wt granularity is to stir 2h behind the nano level 95% alumina-ceramic powder of 10hm, make it be mixed into homogeneous polyphenylene sulfide mixture, then the Preblend of 70%wt polyphenylene sulfide and 30%wt are through β-(3, the 4-epoxycyclohexyl) single fiber diameter was the glass fibre input twin screw extruder of 20um after ethyl trimethoxy silane (A-168) surface treatment agent was processed, be shaped through the twin screw extruder mixing extrusion, cooling, pelletizing forms the finished product composite granule, at last packing, warehouse-in, use.
The various physicalies of the polyphenyl thioether composite material that obtains with aforesaid method will show in Table 1.
The comparative example 1
Be 40,000 with weight-average molecular weight, melt flow index is that 430g/10min and molecular weight distribution are 2.8 linear polyphenylene sulfide resin, adds in the crosslinked device of the heat of oxidation the crosslinked 3h of the heat of oxidation stand-by
In homogenizer, add 60%wt polyphenylene sulfide cross-linked resin, 3%wt phosphorous acid triphenylmethyl methacrylate in ninth of the ten Heavenly Stems oxidation inhibitor, the 37%wt granularity is to stir 3h behind the nano level 95% alumina-ceramic powder of 5nm, make it be mixed into homogeneous polyphenylene sulfide mixture, then the Preblend of 70%wt polyphenylene sulfide and 30%wt are through β-(3, the 4-epoxycyclohexyl) single fiber diameter was the glass fibre input twin screw extruder of 30um after ethyl trimethoxy silane (A-168) surface treatment agent was processed, be shaped through the twin screw extruder mixing extrusion, cooling, pelletizing forms the finished product composite granule, at last packing, warehouse-in, use.
The various physicalies of the polyphenyl thioether composite material that obtains with aforesaid method will show in Table 1.
Embodiment 3
Be 40,000 with weight-average molecular weight, melt flow index is that 451g/10min and molecular weight distribution are 2.7 linear polyphenylene sulfide resin, adds in the crosslinked device of the heat of oxidation the crosslinked 3h of the heat of oxidation stand-by
In homogenizer, add 56%wt polyphenylene sulfide cross-linked resin, 3.3%wt phosphorous acid triphenylmethyl methacrylate in ninth of the ten Heavenly Stems oxidation inhibitor, 3.7%wt polymethylmethacrylate elastomerics, the 37%wt granularity is to stir 2.5h behind the nano level 95% alumina-ceramic powder of 6nm, make it be mixed into homogeneous polyphenylene sulfide mixture, then the Preblend of 65%wt polyphenylene sulfide and 35%wt are through β-(3, the 4-epoxycyclohexyl) single fiber diameter was the glass fibre input twin screw extruder of 25um after ethyl trimethoxy silane (A-168) surface treatment agent was processed, be shaped through the twin screw extruder mixing extrusion, cooling, pelletizing forms the finished product composite granule, at last packing, warehouse-in, use.
The various physicalies of the polyphenyl thioether composite material that obtains with aforesaid method will show in Table 1.
Embodiment 4
Be 4.5 ten thousand with weight-average molecular weight, melt flow index is that 360g/10min and molecular weight distribution are 2.5 linear polyphenylene sulfide resin, adds in the crosslinked device of the heat of oxidation the crosslinked 2.8h of the heat of oxidation stand-by
In homogenizer, add 60%wt polyphenylene sulfide cross-linked resin, 3.4%wt phosphorous acid triphenylmethyl methacrylate in ninth of the ten Heavenly Stems oxidation inhibitor, 4.6%wt polymethylmethacrylate elastomerics, the 32%wt granularity is to stir 3h behind the nano level 95% alumina-ceramic powder of 7nm, make it be mixed into homogeneous polyphenylene sulfide mixture, then the Preblend of 64%wt polyphenylene sulfide and 36%wt are through β-(3, the 4-epoxycyclohexyl) single fiber diameter was the glass fibre input twin screw extruder of 26um after ethyl trimethoxy silane (A-168) surface treatment agent was processed, be shaped through the twin screw extruder mixing extrusion, cooling, pelletizing forms the finished product composite granule, at last packing, warehouse-in, use.
The various physicalies of the polyphenyl thioether composite material that obtains with aforesaid method will show in Table 1.
Embodiment 5
Be 3.8 ten thousand with weight-average molecular weight, melt flow index is that 420g/10min and molecular weight distribution are 2.9 linear polyphenylene sulfide resin, adds in the crosslinked device of the heat of oxidation the crosslinked 3h of the heat of oxidation stand-by
In homogenizer, add 58%wt polyphenylene sulfide cross-linked resin, 3.5%wt phosphorous acid triphenylmethyl methacrylate in ninth of the ten Heavenly Stems oxidation inhibitor, 4.5%wt polymethylmethacrylate elastomerics, the 34%wt granularity is to stir 2.6h behind the nano level 95% alumina-ceramic powder of 8nm, make it be mixed into homogeneous polyphenylene sulfide mixture, then the Preblend of 63%wt polyphenylene sulfide and 37%wt are through β-(3, the 4-epoxycyclohexyl) single fiber diameter was the glass fibre input twin screw extruder of 28um after ethyl trimethoxy silane (A-168) surface treatment agent was processed, be shaped through the twin screw extruder mixing extrusion, cooling, pelletizing forms the finished product composite granule, at last packing, warehouse-in, use.
The various physicalies of the polyphenyl thioether composite material that obtains with aforesaid method will show in Table 1.
The comparative example 2
Be 50,000 with weight-average molecular weight, melt flow index is that 324g/10min and molecular weight distribution are 3.0 linear polyphenylene sulfide resin, adds in the crosslinked device of the heat of oxidation the crosslinked 3h of the heat of oxidation stand-by
In homogenizer, add 51.5%wt polyphenylene sulfide cross-linked resin, 3.5%wt phosphorous acid triphenylmethyl methacrylate in ninth of the ten Heavenly Stems oxidation inhibitor, the 45%wt granularity is to stir 2h behind the nano level 95% alumina-ceramic powder of 10hm, make it be mixed into homogeneous polyphenylene sulfide mixture, then the Preblend of 60%wt polyphenylene sulfide and 40%wt are through β-(3, the 4-epoxycyclohexyl) single fiber diameter was the glass fibre input twin screw extruder of 30um after ethyl trimethoxy silane (A-168) surface treatment agent was processed, be shaped through the twin screw extruder mixing extrusion, cooling, pelletizing forms the finished product composite granule, at last packing, warehouse-in, use.
The various physicalies of the polyphenyl thioether composite material that obtains with aforesaid method will show in Table 1.
Can see by tabulation one among Fig. 2: behind the polymethylmethacrylate elastomer compounds, the melt strength of polyphenylene sulfide (PPS) matrix material has obviously improved, overlap length obviously reduces, impact resistance, anti-bent pleat intensity, tensile strength obviously strengthen, and elongation at break also increases significantly with same type of material.
Owing to melting mixed very even with polyphenylene sulfide after adding polymethylmethacrylate elastomer compounds and phosphorous acid triphenylmethyl methacrylate in ninth of the ten Heavenly Stems compound, can not produce parcel phenomenon or last shape, improved the processing performance of material, so just the balanced technique intensity index that has improved polyphenylene sulfide.
Product indices and employed detection method in Fig. 2 table:
Tensile strength and elongation are all carried out by GB/T1040-1992, and test speed is 10mm/min; Bent pleat intensity is pressed GB/T9341-1988 and is carried out, and resistance to impact shock is pressed GB/T1843-1996 and carried out, and heat-drawn wire is pressed the regulation of GB/T1634-1979 (1989) and carried out.
Performance index by Fig. 2 can be found out, the thermostability of product improves, and commercially available Japanese firm is contained glass fibre 40% like product parallel laboratory test, and its tensile strength, elongation, the bent pleat intensity of glass, resistance to impact shock are respectively 281Mpa, 3.7%, 315Mpa and 18.4j/m2.
After also finding in the experiment to add thicker glass fibre, for example single fiber diameter 35um parallel laboratory test, its resistance to impact shock has obvious enhancing.The elastomeric adding of polymethylmethacrylate also significantly improves the help that forward is provided to tensile strength and the elongation at break of product of the present invention.
After adding polymethylmethacrylate elastomer compounds and phosphorous acid triphenylmethyl methacrylate in ninth of the ten Heavenly Stems compound, polyphenylene sulfide (PPS) matrix material is when thermostability obviously improves, and product overlap length is reduction trend.Since after adding polymethylmethacrylate elastomer compounds and phosphorous acid triphenylmethyl methacrylate in ninth of the ten Heavenly Stems compound, molten mixed very even with polyphenylene sulfide, can not produce parcel phenomenon or last shape yet.The improvement of all these processing condition makes some physical propertiess of product and processing performance obtain comprehensive improvement.
Although embodiments of the invention are with hexamethylene six alkane methyl alcohol polyoxy vinylbenzene ether phosphate amine salt (diethyls, three second), glycerine polyoxy vinylbenzene ether phosphate triethanolamine salt is what provide, also can consider wider Fatty Alcohol(C12-C14 and C12-C18) polyoxy vinylbenzene ether phosphate compounds in the actual production, for example: the aliphatic alcohol polyoxyvinethene phosphate sodium salt, hexamethylene six alkane methyl alcohol polyoxy vinylbenzene ether phosphate amine salt (diethyls, three second), fatty alcohol-ether (7) phosphoric acid ester triethanolamine salt, fatty alcohol-ether (9) phosphoric acid ester triethanolamine salt, octanol phophoric ester MCPH, octanol polyoxyethylene phosphate OPEK, nonyl phenol phosphate sylvite, nonyl phenol ether phosphoric acid monoesters ethanolamine salt, Nonyl pheno (7) ether phosphoric acid, single, dibasic acid esters Nonyl pheno (4-10) ether phosphoric acid, single, dibasic acid esters, the glycerin polyoxyethylene ether phosphoric acid ester, glycerine polyoxy vinylbenzene ether phosphate triethanolamine salt, PAPE, higher alcohols phosphoric acid ester sodium and phosphorylation Viscotrol C sodium salt, Stearinsaeure, the sulfuric ester of glycerol sodium salt, Castor Oil Phosphate Ester Salt, one or more compounds of the phosphate ester salts such as phosphorous acid triphenylmethyl methacrylate in the ninth of the ten Heavenly Stems.
The polymethylmethacrylate elastomer resin compound that adds in the present invention, can reduce the overlap (burr) that polyphenyl thioether composite granulates produces when injection moulded products is shaped, make the surface smoothness height of its molded article and the toughness of injection molded goods, these organoalkoxysilane resins can be vinyltrimethoxy silanes, vinyltriethoxysilane, the styryl triethoxyl silane, the styryl Trimethoxy silane, 3 monomethyl propenyloxy group propyl group methyl dimethoxysilanes, 3 monomethyl propenyloxy group propyl trimethoxy silicanes, 3 monomethyl propenyloxy group propyl group methyldiethoxysilane, 3 monomethyl propenyloxy group propyl-triethoxysilicanes, in the organoalkoxysilanes such as 3-propenyloxy group propyl trimethoxy silicane one or more, especially with vinyltrimethoxy silane, vinyltriethoxysilane, the styryl triethoxyl silane, the styryl Trimethoxy silane, the polymethylmethacrylate elastomerics is better, with the styryl triethoxyl silane, the styryl Trimethoxy silane, the polymethylmethacrylate elastomerics is best.
The objectionable impurities trapping agent that the present invention can also add is inclined to one side zincic acid/zincic acid or its esters compound, and they are: zincic acid, partially zincic acid, inclined to one side zincic acid calcium, partially zincic acid magnesium, partially zincic acid barium, zincic acid calcium, zincic acid magnesium, zincic acid barium, zinc carbonate, etc. contain the compound of zinc, with zincic acid, partially zincic acid is best, and they not only can suppress the generation of corrosives and impurity, can also replenish among the pellet as mineral filler.
Employed fiberglass surface treating agent is to adopt well-known β-(3,4-epoxycyclohexyl) ethyl trimethoxy silane (A-168) surface treatment agent among the present invention.The mineral filler that can also add among the present invention reduces the overlap (burr) of polyphenylene sulfide resin composite material model when injection forming, these mineral fillers can be carbon blacks, nanometer grade silica, nanometer order quartz sand, glass microballon, the nanometer glass powder, Calucium Silicate powder, pure aluminium silicate, talcum, clay, mica, diatomite, the silicate such as wollastonite, ferric oxide, Nano titanium dioxide, zinc oxide, aluminum oxide, light calcium carbonate, nanometer grade calcium carbonate, magnesiumcarbonate, plaster stone, barium sulfate, silicon carbide, silicon nitride, boron nitride etc. are especially with nanometer grade calcium carbonate, nanometer grade silica, Nano titanium dioxide is best.

Claims (3)

1. the manufacture method of a polyphenylene sulfide ceramal, polyphenylene sulfide Preblend behind adding oxidation inhibitor, the ceramic powder is fully mixed in homogenizer, be shaped, form composite granule through cooling, pelletizing with glass fibre input parallel dual-screw extruding machine mixing extrusion again, it is characterized in that, comprise following processing step:
1) be 3-5 ten thousand with weight-average molecular weight, melt flow index is that 300-600g/10min and molecular weight distribution are the linear polyphenylene sulfide resin of 2.5-3.0, adds the crosslinked 2-3h of the heat of oxidation in the crosslinked device of the heat of oxidation;
2) will be 1) in homogenizer, fully mix after adding the weighting agents such as antioxidant, polymethylmethacrylate elastomerics in the polyphenylene sulfide cross-linked resin that obtains, the weight ratio of used antioxidant phosphorous acid triphenylmethyl methacrylate in the ninth of the ten Heavenly Stems and polyphenylene sulfide is 3-3.5: 100; The weight ratio of polymethylmethacrylate elastomerics and polyphenylene sulfide is 3-5: 100, and the weight ratio of ceramics powder and polyphenylene sulfide is 30-40: 100 obtain polyphenylene sulfide Preblend with this;
3) with 2) gained polyphenylene sulfide Preblend 60-70%wt again with through β-(3, the 4-epoxycyclohexyl) the ethyl trimethoxy silane surface treatment agent is processed later 40-30%wt glass fibre input twin screw extruder, forms the finished product composite granule through the shaping of twin screw extruder mixing extrusion, cooling, pelletizing.
2. the manufacture method of described a kind of polyphenylene sulfide ceramal according to claim 1 is characterized in that, described ceramic powder is nano level 95% alumina-ceramic powder, and its granularity is 5-10nm.
3. the manufacture method of described a kind of polyphenylene sulfide ceramal according to claim 1 is characterized in that, described glass fibre single fiber diameter is 20-30um.
CN201110199850.5A 2011-07-18 2011-07-18 Manufacturing method of polyphenylene sulfide ceramic alloy Active CN102888111B (en)

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CN108690353A (en) * 2017-04-11 2018-10-23 合肥杰事杰新材料股份有限公司 A kind of polyphenyl thioether material and preparation method thereof

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108690353A (en) * 2017-04-11 2018-10-23 合肥杰事杰新材料股份有限公司 A kind of polyphenyl thioether material and preparation method thereof

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