Summary of the invention
In view of the deficiencies of the prior art, the present invention intends to provide a kind of polyphenyl ether/styrene composition
And its preparation method and application.The polyphenyl ether/styrene composition is added using hollow metal oxide particle as LDS
Agent, can laser direct forming, compared to directly using metal oxide as the material of LDS additive, polyphenyl provided by the invention
Ether/polyphenylacetylene combination addition LDS additive is less, and coat of metal adhesive force is higher after laser ablation, and mechanical property is more
Good, cost is lower.
To achieve this purpose, the present invention adopts the following technical scheme:
In a first aspect, the present invention provides a kind of polyphenyl ether/styrene composition, including polyphenylene oxide, polystyrene and sky
Heart metal oxide particle;
The hollow metal oxide particle includes cenosphere and the metal oxidation for being coated on the cenosphere surface
Object, the metal oxide are the metal oxides that metal core can be formed by laser activation.
During laser irradiation three dimensional mold interconnecting device forms circuit pattern, the only LDS additive meeting on surface layer
It is activated out metal core, the LDS additive inside plastic device is then not involved in laser activation.The hollow metal oxygen that the present invention uses
Be hollow structure inside compound particle, density is lower, using its as LDS additive polyphenyl ether/styrene composition both
It can guarantee that circuit pattern is activated in material surface under laser irradiation, and the weight of the LDS additive of material internal can be reduced
Amount, reduces cost, and the influence of less additive amount polyphenylene ether/polystyrene substrate mechanical property is also smaller.
As the preferred technical solution of the present invention, the polyphenyl ether/styrene composition includes following weight percent
Component:
Polyphenylene oxide 35-94%;
Polystyrene 5-50%;
Hollow metal oxide particle 0.5-20%.
In the present invention, the weight percent of the polyphenylene oxide can be 35%, 38%, 40%, 45%, 50%, 55%,
58%, 60%, 62%, 65%, 68%, 70%, 72%, 75%, 78%, 80%, 82%, 85%, 88%, 90%, 92% or
94% etc..
The weight percent of the polystyrene can be 5%, 8%, 10%, 12%, 15%, 18%, 20%, 22%,
25%, 28%, 30%, 32%, 35%, 38%, 40%, 42%, 45%, 48% or 50% etc..
The weight percent of the hollow metal oxide particle can be 0.5%, 1%, 1.5%, 2%, 2.5%,
3%, 3.5%, 4%, 4.5%, 5%, 5.5%, 6%, 7%, 8%, 9%, 10%, 12%, 13%, 15%, 16%, 18% or
20% etc..
Preferably, the polyphenyl ether/styrene composition includes following weight percentage components:
Polyphenylene oxide 56-89%;
Polystyrene 10-40%;
Hollow metal oxide particle 1-4%.
As the preferred technical solution of the present invention, the metal oxide is selected from one of oxide or extremely of metal M
Few two kinds of combination, the metal M are selected from titanium (Ti), chromium (Cr), manganese (Mn), iron (Fe), cobalt (Co), nickel (Ni), copper (Cu), niobium
(Nb), one of rhodium (Rh), palladium (Pd), silver (Ag), cerium (Ce), iridium (Ir), platinum (Pt) or gold (Au) or at least two.
Preferably, the metal oxide is copper-chrome black.
Preferably, the metal oxide accounts for the 30-60% of the hollow metal oxide particle quality;Such as it can be
30%, 32%, 35%, 38%, 40%, 42%, 45%, 48%, 50%, 52%, 55%, 58% or 60% etc..
Preferably, the partial size of the hollow metal oxide particle be 0.1-100 μm, such as can be 0.1 μm, 0.5 μm,
1μm、2μm、5μm、8μm、10μm、15μm、20μm、25μm、30μm、35μm、40μm、45μm、50μm、60μm、70μm、80μm、
90 μm or 100 μm etc.;Further preferably 1-50 μm.
Preferably, the density of the hollow metal oxide particle is 1.5-3g/cm3;Such as it can be 1.5g/cm3、
1.8g/cm3、2g/cm3、2.2g/cm3、2.5g/cm3、2.8g/cm3Or 3g/cm3Deng.
As the preferred technical solution of the present invention, the preparation method of the hollow metal oxide particle includes following step
It is rapid:
(a) cenosphere and the corresponding dissolving metal salts of metal oxide are dispersed in water, form mixed liquor;
(b) mixed liquor for obtaining step (a) heats up, and catalyst is then added, and adjust pH to 6-7, is heated to moisture
It evaporates, obtains hollow metal oxide precursor;
(c) the hollow metal oxide precursor for obtaining step (b) is calcined, and obtains the hollow metal oxide
Grain;
It should be noted that " the corresponding metal salt of metal oxide " described in above-mentioned steps (a) refers to metal oxide
In metallic element salt, can be sulfate, nitrate, acetate or chloride etc..The present invention is to cenosphere and metal
The ratio of salt is not specifically limited, and those skilled in the art can be according to cenosphere and metal oxygen in hollow metal oxide particle
The ratio of compound is calculated in conjunction with general technology knowledge.
Preferably, heating described in step (b) is to be warming up to 40-100 DEG C;Such as it can be 40 DEG C, 45 DEG C, 50 DEG C, 55
DEG C, 60 DEG C, 65 DEG C, 70 DEG C, 75 DEG C, 80 DEG C, 85 DEG C, 90 DEG C, 95 DEG C or 100 DEG C etc..
Preferably, catalyst described in step (b) is urea and/or dodecyl benzene sulfonic acid sodium salt.
Preferably, the method that catalyst is added described in step (b) is to be added dropwise.
Preferably, the temperature of calcining described in step (c) is 500-1200 DEG C, such as can be 500 DEG C, 520 DEG C, 550
℃、580℃、600℃、620℃、650℃、680℃、700℃、720℃、750℃、780℃、800℃、850℃、900℃、
950 DEG C, 1000 DEG C, 1050 DEG C, 1100 DEG C, 1150 DEG C or 1200 DEG C etc.;Further preferably 500-800 DEG C.
Preferably, the time of the calcining is 1-5h;Such as can be 1h, 1.2h, 1.5h, 1.8h, 2h, 2.2h, 2.5h,
2.8h, 3h, 3.2h, 3.5h, 3.8h, 4h, 4.2h, 4.5h, 4.8h or 5h etc..
As the preferred technical solution of the present invention, the cenosphere is that hollow glass micropearl or hollow silicon dioxide are micro-
Pearl.
As the preferred technical solution of the present invention, the polyphenyl ether/styrene composition further includes 0.02-2wt% (example
As 0.02wt%, 0.05wt%, 0.08wt%, 0.1wt%, 0.2wt%, 0.3wt%, 0.4wt%, 0.5wt%, 0.6wt%,
0.7wt%, 0.8wt%, 0.9wt%, 1wt%, 1.2wt%, 1.5wt%, 1.8wt% or 2wt% etc.) antioxidant.
Preferably, the antioxidant is the compound of Hinered phenols antioxidant and phosphite ester antioxidant.
The Hinered phenols antioxidant and the mass ratio of phosphite ester antioxidant are preferably 1:1.
Second aspect, the present invention provides a kind of preparation method of above-mentioned polyphenyl ether/styrene composition, including walks as follows
It is rapid:
(1) by polyphenylene oxide, polystyrene and optionally antioxidant mixing, premix is formed;
(2) premix and hollow metal oxide particle melting extrusion obtained step (1), obtain the polyphenylene oxide/
Polyphenylacetylene combination.
It should be noted that " optionally " referring to described in above-mentioned steps (1) with and without when polyphenylene oxide/polyphenyl second
When adding antioxidant in ene compositions, then it is mixed with polyphenylene oxide, polystyrene;When in polyphenyl ether/styrene composition
When not adding antioxidant, then directly by polyphenylene oxide, polystyrene and hollow metal oxide particle melting extrusion.
As the preferred technical solution of the present invention, the preparation method further include: will be to the polyphenyl before step (1)
Ether and the polystyrene are dried.
The method of the drying process is preferably in 90-110 DEG C of drying 3-5h.
Preferably, mixing described in step (1) is carried out in mixing machine.
Preferably, the revolving speed of the mixing machine be 300-500r/min, such as can be 300r/min, 320r/min,
350r/min, 380r/min, 400r/min, 420r/min, 450r/min, 480r/min or 500r/min etc.;The mixing
Time is 10-20min, such as can be 10min, 12min, 13min, 15min, 16min, 18min or 20min etc..
Preferably, melting extrusion described in step (2) is carried out in parallel double-screw extruder.
Preferably, premix described in step (2) is added from the main spout of the parallel double-screw extruder, the sky
Heart metal oxide particle is added from the 6th area of the parallel double-screw extruder.
Preferably, area's temperature of the parallel double-screw extruder is 250-270 DEG C, such as can be 250 DEG C, 252
DEG C, 255 DEG C, 258 DEG C, 260 DEG C, 262 DEG C, 265 DEG C, 268 DEG C or 270 DEG C etc..
Two area's temperature are 270-290 DEG C, such as can be 270 DEG C, 272 DEG C, 275 DEG C, 278 DEG C, 280 DEG C, 282 DEG C, 285
DEG C, 288 DEG C or 290 DEG C etc.;
Three area's temperature are 270-290 DEG C, such as can be 270 DEG C, 272 DEG C, 275 DEG C, 278 DEG C, 280 DEG C, 282 DEG C, 285
DEG C, 288 DEG C or 290 DEG C etc.;
4th area are 270-290 DEG C of temperature, such as can be 270 DEG C, 272 DEG C, 275 DEG C, 278 DEG C, 280 DEG C, 282 DEG C, 285
DEG C, 288 DEG C or 290 DEG C etc.;
Five area's temperature are 270-295 DEG C, such as can be 270 DEG C, 272 DEG C, 275 DEG C, 278 DEG C, 280 DEG C, 282 DEG C, 285
DEG C, 288 DEG C, 290 DEG C, 292 DEG C or 295 DEG C etc.;
Six area's temperature are 270-295 DEG C, such as can be 270 DEG C, 272 DEG C, 275 DEG C, 278 DEG C, 280 DEG C, 282 DEG C, 285
DEG C, 288 DEG C, 290 DEG C, 292 DEG C or 295 DEG C etc.;
Seven area's temperature are 270-295 DEG C, such as can be 270 DEG C, 272 DEG C, 275 DEG C, 278 DEG C, 280 DEG C, 282 DEG C, 285
DEG C, 288 DEG C, 290 DEG C, 292 DEG C or 295 DEG C etc.;
Eight area's temperature are 270-295 DEG C, such as can be 270 DEG C, 272 DEG C, 275 DEG C, 278 DEG C, 280 DEG C, 282 DEG C, 285
DEG C, 288 DEG C, 290 DEG C, 292 DEG C or 295 DEG C etc.;
Nine area's temperature are 270-295 DEG C, such as can be 270 DEG C, 272 DEG C, 275 DEG C, 278 DEG C, 280 DEG C, 282 DEG C, 285
DEG C, 288 DEG C, 290 DEG C, 292 DEG C or 295 DEG C etc.;
Die head temperature is 270-295 DEG C, such as can be 270 DEG C, 272 DEG C, 275 DEG C, 278 DEG C, 280 DEG C, 282 DEG C, 285
DEG C, 288 DEG C, 290 DEG C, 292 DEG C or 295 DEG C etc..
Preferably, residence time of the material in the parallel double-screw extruder is 1-3min;Such as can be 1min,
1.2min, 1.5min, 1.8min, 2min, 2.2min, 2.5min, 2.8min or 3min etc..
As the preferred technical solution of the present invention, the preparation method includes the following steps:
(1) polyphenylene ether and polystyrene are dried, and are then added to the mixer with antioxidant, in 300-
10-20min is mixed under the revolving speed of 500r/min, forms premix;
(2) premix for obtaining step (1) is added from the main spout of parallel double-screw extruder, hollow metal oxidation
Composition granule is added from the 6th area of the parallel double-screw extruder, and the area's temperature for controlling the parallel double-screw extruder is
250-270 DEG C, two area's temperature are 270-290 DEG C, and three area's temperature are 270-290 DEG C, and 4th area are 270-290 DEG C of temperature, five Qu Wen
Degree be 270-295 DEG C, six area's temperature be 270-295 DEG C, seven area's temperature be 270-295 DEG C, eight area's temperature be 270-295 DEG C, nine
Area's temperature is 270-295 DEG C, and die head temperature is 270-295 DEG C, residence time of the material in the parallel double-screw extruder
For 1-3min, the polyphenyl ether/styrene composition is obtained after melting extrusion.
The third aspect, the present invention provide a kind of purposes of above-mentioned polyphenyl ether/styrene composition, the polyphenylene oxide/poly-
S compositions are used for three dimensional mold interconnecting device.
Compared with prior art, the invention has the following advantages:
Polyphenyl ether/styrene composition provided by the invention using hollow metal oxide particle as LDS additive,
Can laser direct forming, compared to directly using metal oxide as the material of LDS additive, polyphenylene oxide provided by the invention/
The LDS additive of polyphenylacetylene combination addition is less, and coat of metal adhesive force is higher after laser ablation, hollow metal oxide
When particle additive amount reaches 3wt%, coat of metal adhesive force can reach 5B rank;Mechanical property is more preferable, and cost is lower.