Preferred embodiment of the present invention
The present invention provides a kind of resin combinations, including poly arylidene thio-ester and cyclohexanedimethanol to support dimethylene
Ester, it includes the repetitive unit that formula 1 indicates that the cyclohexanedimethanol, which supports dimethylene ester,:
[formula 1]
The resin combination of the present invention has a small amount of outgassings of 300ppm or less, and it is viscous to obtain excellent metal
Attached performance.Specifically, the resin combination has the release quantity of 150-300ppm.
The chlorinity of the resin combination is 300ppm or less, and includes the by-product of a small amount of salt form, to not
The performance of electronic product can be reduced.Particularly, the chlorinity of the resin combination is 200ppm or less, 100ppm or more
It is few, for example, more than 0 to less than or be equal to 100ppm, be 50ppm or less more particularly.
It is 80MPa or higher, in particular 80- according to the tensile strength values of the resin combinations measured of ISO 527
150MPa。
According to the metal adhesion intensity value of the resin combinations measured of ASTM D 3163 be 60MPa or higher, especially
Ground is 60-80MPa.
In addition, including specular components (specular component-included, SCI) mould according to D65 light sources
The L values for the resin combination that formula measures are 89 or higher, in particular 90-93.L values are higher, and whiteness is better.
Metal adhesion intensity value of the resin combination measured according to ASTM D 3163 after anodic oxidation be
55MPa or higher, in particular 55-80MPa.
The resin combination measured according to the SCI patterns of D65 light sources is carrying out sun by using the chemical method of acid
L values after the oxidation of pole are 88 or higher, in particular 88-93.
Hereinafter, the present invention is described in detail.
The resin combination of the present invention includes poly arylidene thio-ester.
The poly arylidene thio-ester includes the iodine being bonded with its main chain and free-iodine, particularly, the iodine that is bonded with main chain and free
The amount of iodine can be 10-10,000ppm.The amount of the iodine and free-iodine that are bonded with main chain can be by being heat-treated poly- virtue at high temperature
It thioether sample and is measured using ion chromatography standard measure.Free-iodine is to polymerize two iodo aromatic compounds and element sulphur
It generates in the process, and includes iodine molecule, iodide ion, iodine free radical etc., general holding is mutually changed with the poly arylidene thio-ester finally generated
Credit from state.
Poly arylidene thio-ester can be by carrying out melt polymerization to the reactant comprising two iodo aromatic compounds and element sulphur
To prepare.The two iodo aromatic compounds that can be used in the polymerisation can be selected from diiodo-benzene (DIB), diiodonaphthalene,
At least one of the group that diiodide, diiodo- bis-phenol and diiodobenzophenone are constituted, but an embodiment of the present invention is not limited to
This.In addition, two iodo aromatic compounds may include wherein substituted base alkyl or two iodo aromatic series of sulfuryl substitution
Close two iodo aromatic compounds of the atom containing such as oxygen and nitrogen in object or aromatic radical.Further, two iodo aromatic series
Compound can have the various isomers of diiodide, and wherein change of the iodine in para-linkage according to the bonding position of iodine
Object is closed, for example, paradiiodobenzene, 2,6- diiodonaphthalenes and 4,4'- diiodides are more particularly suitable.
The form of the element sulphur reacted with two iodo aromatic compounds is not particularly limited.Element sulphur is usually with eight sulphur of ring
(S8) form exists, wherein 8 atoms connect at room temperature.If not this form, it is nonetheless possible to use commercially available solid or
The sulphur of liquid form and be not particularly limited.
In addition, the mixture of two iodo aromatic compounds and reactant can further include polymerization initiator, stabilizer
Or mixtures thereof.Polymerization initiator may include selected from 1,3-, bis- iodo- 4- nitrobenzenes, mercaptobenzothiazoler, 2,2'-, bis- thio benzos
At least one of the group that thiazole, cyclohexylbenzothiazole sulfenamide and butyl benzo thiazolesulfenamide are constituted, but it is unlimited
In this.
Stabilizer can use without limitation, as long as it is common stabilizer in resin polymerization reaction.
Meanwhile in melt polymerization process, polymerization quencher can be added.Polymerization quencher is not particularly limited, only
Want it that can remove the iodine group for including in the polymer of polymerization to stop polymerization.Specifically, polymerization quencher can be
Selected from diphenyl sulfide, diphenyl ether, diphenylbenzophenone, bisbenzothiazole disulphide, single iodine aryl compound, benzo thiophene
At least one of the group that azoles, benzothiazole sulfenamide, thiurams (thiurams) and dithiocarbamate are constituted.
More specifically, polymerization quencher can be selected from iodine biphenyl, iodophenol, Iodoaniline, iodobenzophenone, 2- sulfydryl benzo thiophenes
Azoles, 2,2'- dithiobisbenzothiazoles, N cyclohexyl 2 benzothiazole sulfenamide, the thio benzothiazole of 2- morpholinoes, N,
N- dicyclohexyls -2-[4-morpholinodithio sulfenamide, tetra methylthiuram list sulfide, tetramethyl thiuram disulfide, diformazan
At least one of the group that base zinc dithiocarbamate, zinc diethyl dithiocarbamate and diphenyl disulfide are constituted.
The molecular weight of target poly arylidene thio-ester can be considered to determine in the decanting point of polymerization quencher.For example, polymerization quencher
Can by reaction consume about 70-100wt% be included in initial reactant in two iodo aromatic compounds when
Carve injection.
In addition, the condition of melt polymerization is not particularly limited, as long as can cause comprising diiodo- aromatic compounds and sulphur member
The polymerization of the reactant of element.For example, melt polymerization can carry out at raised temperature and the pressure condition of reduction.At this
In the case of kind, the initial reaction condition held in the palm from 180-250 DEG C and 50-450 can increase temperature to 270-350 DEG C and can drop
The end reaction condition that low-pressure is held in the palm to 0.001-20, and the reaction can carry out about 1-30 hour.More specifically, this is poly-
It is carried out under the conditions of conjunction reaction can be about 280-300 DEG C in temperature, pressure is about the end reaction of 0.1-1 supports.
Meanwhile the method for preparing poly arylidene thio-ester can further comprise before melt polymerization:Melting mixing includes
Diiodo- from generation to generation the reactant of aromatic compound and element sulphur the step of.The condition of melting mixing is not particularly limited, as long as instead
Answer object that can be melt-mixed.For example, the melting mixing step can be at 130-200 DEG C, especially 160-190 DEG C of temperature
Degree is lower to carry out.The melting mixing step before melt polymerization can allow subsequent melt polymerization easily into
Row.
According to another implementation of the invention prepare the method for poly arylidene thio-ester, which can be with
It is carried out in the presence of nitrobenzene catalyst.In addition, when carrying out melting mixing in taking a step forward for above-mentioned melt polymerization
When step, nitrobenzene catalyst can be added in the melting mixing step.For example, nitrobenzene catalyst may include but
It is not limited to bis- iodo- 4- nitrobenzenes of 1,3- or the iodo- 4- nitrobenzenes of 1-.
Different from customary preparation methods, thus obtained poly arylidene thio-ester is nearly free from the by-product of salt form.For example, this
The chlorinity of the poly arylidene thio-ester of invention is 300ppm or lower, especially 200ppm or lower, more particularly 100ppm or lower.
The fusing point of the poly arylidene thio-ester can be about 265-290 DEG C, about 270-285 DEG C, or about 275-283 DEG C.In addition, this is poly-
The number-average molecular weight of aromatic sulfide can be about 5,000-50,000, about 8,000-40, and 000, or about 10,000-30,000.Into one
Step ground, the poly arylidene thio-ester can be defined as opposite with the dispersion degree of about 2.0-4.5, about 2.0-4.0, or about 2.0-3.5
In the weight average molecular weight of number-average molecular weight.
The melt viscosity of the poly arylidene thio-ester measured at 300 DEG C with rotatingdisc viscometer can be about 10-50,000
Pool, about 100-20,000 pool, or about 300-10,000 pool.
Meanwhile resin combination of the invention includes that cyclohexanedimethanol supports dimethylene ester (PCT).This is poly- to benzene
Dioctyl phthalate cyclohexalene dimethylene ester includes the repetitive unit that following formula 1 indicates.
[formula 1]
Including the PCT of the repetitive unit indicated by formula 1 can have 10,000-200,000 or 30,000-70,000 weight
The inherent viscosity (IV) of average molecular weight and 0.1-1dl/g or 0.5-0.8dl/g.In addition, when use spectrocolorimeter according to
When being measured comprising specular components pattern of D65 light sources, the L values of the PCT are 80 or higher, in particular 85 or more
It is high;B values are 10 or lower, in particular 6 or lower.
The PCT can be prepared by customary preparation methods, including by include germanium compound catalyst be injected into it is diolation
The step of closing in the mixture of object and dicarboxylic acids and stirring to carry out esterification and polycondensation reaction.
Based on the PAS of 100 parts by weight, the resin combination can include 0.5-50 parts by weight, 1-40 parts by weight or 3-
The PCT of 30 parts by weight.In the case where the amount based on 100 parts by weight PAS, PCT is 0.5 parts by weight or more, metallic adhesion
It may become excellent with whiteness, and be 50 parts by weight or less in the amount of the PCT, resin group may not occur
Close the deterioration of the mechanical strength of object.
According to embodiment of the present invention, the resin combination can obtain excellent whiteness and metal adhesion
Property, this is that traditional pas resin composition institute is inaccessiable, and can also obtain high whiteness after anodic oxidation and retain
Rate and high metal adhesiveness.
In addition, the resin combination of the present invention can also include selected from phenoxy resin (phenoxy resin), elasticity
Body, filler, shock absorber fluid (shock absorber), adhesiveness reinforcing agent, stabilizer, pigment, plasticizer, lubricant and nucleating agent
At least one of component.
The resin combination may further include phenoxy resin, and the phenoxy resin by further including
The metallic adhesion of the resin combination can be enhanced.Specifically, the weight average molecular weight of the phenoxy resin can be 10,
000-250,000, glass transition temperature is 50-130 DEG C.More specifically, the phenoxy resin can be indicated with following formula 2.
More specifically, the phenoxy resin may include bisphenol-A (BPA), and can be with 20,000-220,000 Weight-average molecular
Amount and 60-120 DEG C of glass transition temperature.
[formula 2]
In formula 2, n is the integer of 100-900.Specifically, n can be 100-700 integer, the integer of 100-500,
The integer of 100-300, the integer of 200-300 or the integer of 300-500.
The end of the phenoxy resin can be replaced by hydroxyl and/or carboxyl.
Based on the PAS of 100 parts by weight, the resin combination may include the phenoxy resin of 1-75 parts by weight.Particularly,
Based on the PAS of 100 parts by weight, the addition of the phenoxy resin can be 3-15 parts by weight.
Elastomer can be additionally incorporated in the resin combination of the present invention, it is tough to assign the resin combination
Property, and generate the effect prevented because leading to the interfacial separation between resin and metal after metal adhesion due to temperature change.Make
For elastomer, can use selected from polyvinyl chloride elastomer, ethylene octane copolymer, polyurethane elastomer, polyesters bullet
Property body, polyamide-based elastomer, polybutadiene elastomer and glycidyl methacrylate, methacrylate and
At least one of the group that the terpolymer of ethylene is constituted thermoplastic elastomer (TPE).Particularly, the elastomer can be methyl
The terpolymer of glycidyl acrylate, methacrylate and ethylene.
Based on the PAS of 100 parts by weight, the resin combination may include 1-75 parts by weight, especially 3-35 parts by weight
Elastomer.
As filler, it can use and be selected from glass fibre, carbon fiber, boron fibre, bead, sheet glass, talcum powder and carbon
At least one of the group that sour calcium is constituted, and glass fibre is preferred.The glass fibre can be the glass of silane treatment
Fiber, and the silane can be selected from epoxy silane and amino silane and combinations thereof, and particularly, can use at epoxy silane
The glass fibre of reason.
The filler can be the form of powder or thin slice, but not limited to this.
Based on the PAS of 100 parts by weight, the content of the filler can be 5-250 parts by weight, preferably 10-150 weight
Part.
The pigment can be organic or inorganic pigment well known in the art, and can be selected from, for example, zinc sulphide
(ZnS), zinc oxide (ZnO), titanium dioxide (TiO2) and combinations thereof.Particularly, the pigment can be zinc sulphide (ZnS).
Based on the PAS of 100 parts by weight, the content of the pigment can be 0.1-50 parts by weight, preferably 0.3-25 weight
Part.
The stabilizer can be, such as antioxidant, light stabilizer and combinations thereof.In addition, based on 100 parts by weight
The content of PAS, the stabilizer can be 0.1-10 parts by weight.
The example of antioxidant may include any material for assigning the resin combination high-fire resistance and thermal stability
Material is without especially limiting.It is, for example, possible to use phenol antioxidant, amine antioxidants, sulphur class antioxidant and Phosphorus anti-
Oxidant.As phenol antioxidant, it is preferable to use hindered phenol compound.The specific example of phenol antioxidant is four (sub-
Methyl -3- (3,5- di-tert-butyl-hydroxy phenyl) propionic ester) methane, bis- [3- (3, the 5- di-t-butyl -4- hydroxyls of thio diethylene
Base phenyl) propionic ester], N, N'- it is bis- [3- (3,5- di-tert-butyl-hydroxy phenyls) propiono) hexamethylene diamine etc..It is Phosphorus anti-oxidant
The example of agent is three (2,4- di-tert-butyl-phenyls) phosphates, O, O'- octacosyl pentaerythrites bis- (phosphite esters), double
Bis- four oxygen of (2,4- di-t-butyls phenoxy group) -2,4,8,10- of (2,4- di-tert-butyl-phenyls) pentaerythritol diphosphites, 3,9-
Miscellaneous -3,9- two phospha spiral shell [5.5] hendecane etc..
Light stabilizer can be any material that can be absorbed and stop ultraviolet light without especially limiting;And can be,
For example, benzophenone compound;Salicylic acid ester type compound;Benzotriazole compound;Acrylonitrile compound;With purple
Other compounds of outside line assimilation effect, such as conjugated compound;The compound of free radical, such as hindered amine compound can be captured
And hindered phenol compound, or combinations thereof.If simultaneously using with ultraviolet radiation absorption effect compound and can capture from
By the compound of base, then high ultraviolet radiation absorption and blocking effect can be obtained.
The resin combination can further include the lubricant for enhancing mouldability.Particularly, alkyl lubricates
Agent can be used for preventing the friction between resin and Mold Metal, and allow readily to be detached from (releasable property) etc. from mold.Hydrocarbon
Base lubricating agent can be selected from paraffin, polyester (PE) wax, polypropylene (PP) wax, oxidation polyester wax and combinations thereof without especially limiting.
In addition, the PAS based on 100 parts by weight, lubricant can be added to institute with 0.1-10 parts by weight, the amount of preferably 0.5-5 parts by weight
It states in resin combination.
Meanwhile the present invention can provide a kind of moulding article manufactured by above-mentioned resin combination.
Resin combination can be subjected to casting and forming according to methods known in the art, such as twin shaft squeezes out, with manufacture
With excellent metallic adhesion, whiteness and acid proof moulding article, and can be used in various applications.
The moulding article can have various forms, including film, sheet material or fiber.The moulding article can be note
Mould product, extrudate or blow-molded article.In the case of injection molding, for crystallization, the temperature of mold can be about 130
DEG C or higher.In the case where moulding article is film, sheet-form, they can be made to various films or sheet material, such as
No yield point, uniaxial orientation or biaxially oriented film or sheet material.In the case where moulding article is fiber, the moulding article
It may be used as the fiber of No yield point, stretch fiber or super drawing fiber etc., it is also possible to make fabric, knitwear, non-woven fabrics (spunbond
Cloth, fusion spray cloth, staple fibre cloth), rope or net.
The above moulding article may be used as electrically or electronically part, such as need the computer fittings of metal adhesion, building
Material, auto parts, machine parts or basic item, and with chemicals or area that the industrial fiber with chemical resistance contacts
The coating in domain.
The embodiment of the present invention
The present invention is more fully described below in reference to each embodiment.Following implementation is intended to further illustrate this
Invention, but the scope of the present invention is not limited thereto.
Preparation example:Prepare PPS
Equipped with the thermocouple for measuring inside reactor temperature and the vacuum for filling nitrogen and manufacture vacuum
To include that the paradiiodobenzene (p-DIB) of 5,130g and the mixture of 450g sulphur are heated to 180 DEG C in the 5L reactors of pipeline,
To be completely melt and mix.By initiation reaction under conditions of 220 DEG C and 350 support, and it is stepped up temperature and reduces pressure 4
The final condition that hour holds in the palm to 300 DEG C and 0.6-0.9, and by injecting 7 sulphur and each 19g, make mixed reactant
Carry out polymerisation.When polymerisation proceeds to about 80% (degree of polymerisation by " (actual viscosity/target viscosities) ×
100 " determine), that is, relative ratios of the actual viscosity relative to target viscosities.It is measured by being sampled during polymerization current viscous
Degree, and target viscosities are set as 2,000 pool), the diphenyl disulfide of 35g is added as polymerization quencher, and in nitrogen atmosphere
Under carry out reaction 10 minutes.Pressure is down to 0.5 support or lower gradually to generate vacuum, and is terminated after reaching target viscosities anti-
It should be to synthesize poly arylidene thio-ester (PPS) resin in its main chain terminal not hydroxyl.Use small-sized pelleter (small strand
Cutter graininess) is made in resin after reaction.
The fusing point (Tm) of PPS resin, number-average molecular weight (Mn), polydispersity index (PDI) are measured by the following method and are melted
Body viscosity (hereinafter will be called " MV ").As measurement as a result, understand PPS resin Tm be 280 DEG C, Mn 17,420, PDI
It is moored for 2.8, MV 2,150, the content of the iodine and free-iodine that are bonded with main chain is 200ppm.
Fusing point (Tm)
Fusing point is measured using differential scanning calorimeter (DSC), while being increased temperature from 30 DEG C with 10 DEG C/min of rate
To 320 DEG C, 30 DEG C are cooled to, temperature is then increased to 320 DEG C from 30 DEG C with 10 DEG C/min of rate.
Number-average molecular weight (Mn) and polydispersity index (PDI)
So that PPS resin is dissolved in 1- chloronaphthalenes by being stirred 25 minutes at 250 DEG C, make its a concentration of 0.4wt%, prepares
Obtain sample.Later, by the poly arylidene thio-ester with different molecular weight with the flow rate of 1mL/min, and in High Temperature Gel Permeation
It is detached successively in the column of chromatography (GPC) system (210 DEG C), and corresponds to the poly arylidene thio-ester isolated using RI detectors measures
Molecular weight intensity.After preparing calibration curve using the standard sample (polystyrene) of known molecular amount, made from calculating
The opposite number-average molecular weight (Mn) and polydispersity index (PDI) of PPS resin.
Melt viscosity (Melt viscosity, MV)
Using rotatingdisc viscometer melt viscosity is measured at 300 DEG C.When being measured by frequency scanning method, angular frequency
Rate is measured as 0.6 to 500rad/s, and the viscosity at 1.84rad/s is defined as melt viscosity (MV).
The content (ppm) of the iodine and free-iodine that are bonded with main chain
Using the sample prepared by automatic conflagration stove (AQF) come measure the iodine being bonded with main chain in PPS resin and
The amount (ppm) of free-iodine wherein burning at 1000 DEG C PPS resin using smelting furnace, and by iodide ion and is dissolved in distilled water
In, and the calibration curve analyzed using ion chromatography is first passed through in advance.
Embodiment 2-5 and comparative example 1
PPS resin composition is prepared according to identical step described in embodiment 1, the difference is that component and its dosage
As shown in table 2 below.
Comparative example 2
PPS resin composition is prepared according to identical step described in embodiment 1, the difference is that using solution is passed through
PPS (manufacturers made from polymerisation:Celanese Co., ProductName:0205P4, line style PPS, hereinafter will be called
" PPS1 ") replace PPS obtained in preparation example as PPS resin.
Comparative example 3
PPS resin composition is prepared according to identical step described in embodiment 1, the difference is that using solution is passed through
PPS (manufacturers made from polymerisation:Solvay Co., ProductName:P6 is crosslinked PPS, hereinafter will be called " PPS2 ") conduct
PPS resin replaces PPS obtained in preparation example.
Comparative example 4
PPS resin composition is prepared according to identical step described in embodiment 1, the difference is that component and its dosage
As shown in table 2 below, and PCT resins are not used.
Comparative example 5
PPS resin composition is prepared according to identical step described in embodiment 1, the difference is that component and its dosage
As shown in table 2 below.
Comparative example 6
PPS resin composition is prepared according to identical step described in embodiment 1, the difference is that using poly- to benzene two
Formic acid glycol ester (PET, manufacturer:SK Chemicals Co., ProductName:BB 8055) replace PCT resins.
The manufacturer of component used in embodiment 1-5 and comparative example 1-6 is summarized and shown in the following table 1.
[table 1]
Experimental example
The physical property of PPS resin composition obtained in embodiment and comparative example is tested as follows.As a result as follows
Shown in table 2.
First, PPS resin composition obtained in embodiment and comparative example is prepared into injection molding examination at 310 DEG C by being molded
Sample (injection molded specimens).
(1) release quantity
By the aluminium sample (width of etched processing:70mm, length:18mm, height:Two steps 2mm) being placed in injection molding machine
The fixing mould of mold and between moving moulds.Each PPS resin composition obtained in embodiment and comparative example is provided
In the two steps mold, and insertion is injected into 80 tons of Engel extruders, injection rate 50mm/s, and injection pressure is
120MPa, mold temperature are 150 DEG C.Then, by sample and mold separation to manufacture the sample for measuring metal adhesion intensity
(width:70mm, length 10mm, height:3mm) (Fig. 1).Later, the injection-molded test specimens of 2g are placed in the sealed vial of 20mL.
After the bottle is sealed, it is heated 30 minutes at 260 DEG C using head space (head space, HS) equipment, and will thus produce
Raw gas is automatically transported in gas chromatograph-mass spectrometer (GC/MS) equipment.Then, with capillary column detach each component with into
Row qualitative analysis is used in combination benzothiazole as the constituent content in standard substance quantitative analysis sample.
(2) chlorinity
By each injection-molded test specimens of the 50mg of the PPS of preparation example and the PPS1 or PPS2 of the polymerisation in solution (injection molding of above-mentioned (1)
Sample) organic material while humidified at 1000 DEG C by its completely burned, and using automatic fast stove (AQF) by burning
In gas collection to absorbent solution (hydrogen peroxide of 900ppm).Acquired solution is automatically injected in ion chromatography, and is measured
The chlorinity of injection-molded test specimens.
(3) tensile strength
The tensile strength of injection-molded test specimens is measured according to 527 methods of ISO.
(4) metal adhesion intensity
The metal adhesion intensity of injection-molded test specimens is measured according to ASTM D 3163.
(5) L values
Specular components are included according to D65 light sources using spectrocolorimeter (Konica Minolta, 3600D)
(SCI) pattern measures L values.L values are higher, and whiteness is better.
(6) anodic oxidation reactions
Molded sample in above-mentioned (1) is immersed in sodium hydroxide (NaOH) solution 30 seconds at 50 DEG C, is placed in volume
Than being 1:2 minutes in the mixed solution of the aqueous sulfuric acid of 7 98wt% and the phosphate aqueous solution of 84wt%.Later, by
So that the electric current of 20V is flowed 20 minutes in dilution heat of sulfuric acid to carry out oxidation process at room temperature, and carries out washing process.By with
(1) identical method measures metal adhesion intensity in, and measures L values by the identical method with (5), and measures anodic oxidation
Difference between the two front and back values.As can be seen that the difference is smaller, acidity is better.
[table 2]
As shown in table 2, the metal adhesion intensity of resin combination of the invention is 60-70MPa, and is significantly better than and includes
The resin combination 1-50MPa of the comparative example 1 of excess glass fiber.In addition, with comparative example 2 and 3 phases comprising PPS1 or PPS2
Than, including in preparation example PPS obtained embodiment 1-5, the release quantity shown reduces about four times.Further, implement
The chlorinity of example 1-5 is 35ppm or less, but the chlorinity of comparative example 2 is higher and be 891ppm, and the chlorinity of comparative example 3 is
1562ppm.In addition, for embodiment 1-5, the L values after anodic oxidation are 90 or higher, but comparative example 2 be 90 or
It is lower, and its whiteness reduces rapidly.
Moreover, when compared with the comparative example 4 not comprising PCT resins, the resin combination of embodiment 1-5 shows to improve
Metallic adhesion, metal adhesion intensity be 60-70MPa.However, the metal adhesion intensity of comparative example 4 is 55MPa, and right and wrong
It is often low.
In addition, the tensile strength of the comparative example 5 of excess PCT resins, which is wherein added, to be reduced.Meanwhile wherein comprising PCT is replaced
The comparative example 6 of the PET resin of resin shows high metallic adhesion but low L values.Compared with embodiment 1-5, anodic oxidation
The L values afterwards significantly reduce.
Therefore, resin combination of the invention shows the release quantity, excellent whiteness, acid resistance and the metal adhesion that reduce
Property, therefore can be used for various fields, including portable phone, electronic component, auto parts etc., they can by insert injection moulding at
Type and it is integrated.