CN1438267A - Impact-resistant transparent styron composition - Google Patents
Impact-resistant transparent styron composition Download PDFInfo
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- CN1438267A CN1438267A CN 02120639 CN02120639A CN1438267A CN 1438267 A CN1438267 A CN 1438267A CN 02120639 CN02120639 CN 02120639 CN 02120639 A CN02120639 A CN 02120639A CN 1438267 A CN1438267 A CN 1438267A
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Abstract
The invention provides a shock-resistant transparent styrene resin combination as well as the making method. It makes the continuous block polymerization on styrene monomer (a1), (methyl) aykyl acrylate (a2) and styrene butadiene block copolymer (b) to get the combination, (b) forms rubber particles, the copolymer (A) of (a1) and (a2) forms the base material, the Z average molecular weight of (A): Mz=22X10 to the power 4 - 28X10 to the power 4, the average diameter of the particles is 0.3-2.0 micron m, and the content of the block is 2.0-7.5%.
Description
Technical field
The invention relates to and have the impact-resistant transparent styron composition that excellent formability and the transparency and shock-resistance and inflexible balance are good, be used for film or thin slice purposes.That is, transparent styron composition of the present invention, formability is fine, and, as thin slice moulding product because shock-resistance and inflexible balance are extremely good, so used for packing foods dish, lid material, cup, various hold in the purposes such as usefulness dish, travelling belt exceedingly useful.
Technical background
In the past, for the content in the dish that can see plastic containers etc., though most container that uses the biaxial stretch-formed thin slice of polystyrene systems, the problem that these containers exist was because poor impact resistance is very easily damaged, and the edge of container produces cutting wound etc.
Therefore, for example, as the resin that has the transparency and shock-resistance simultaneously, a kind of styrene resin composite of modified rubber is disclosed in No. 3151481 communique of special permission, this resin combination is as dispersed particle with rubber-like elastic body, make it and styrenic monomers and (methyl) acrylic ester monomer carry out graft polymerization again, with styrenic monomers and the monomeric multipolymer of (methyl) acrylic ester as external phase.
Yet, the rubber-modified styrene resin composition of putting down in writing in No. 3151481 communique of above-mentioned special permission is in requiring the very good purposes of transparency practical intensity fine, that impact strength especially with the hammer falling impact strength is representative, for example, container cover one class as thin slice moulding product, need in the purposes of intensity in lower part, rigidity is not enough, can produce distortion etc. when portion increases the weight of from container, so exist shortcoming in practicality.With regard to the transparency, do not reach the ideal level as thin slice moulding product yet.
Summary of the invention
The problem that the present invention will solve, it is good and have the shock-resistant transparent styron composition and a manufacture method thereof of the good transparency just to provide a kind of shock-resistance and inflexible balance.
The inventor is for solving above-mentioned problem, further investigate, found that, by matrix be dispersed in the impact-resistant transparent styron composition that the rubber-like particle in this matrix forms, above-mentioned matrix is formed by the multipolymer (A) of styrenic monomers (a1) and (methyl) alkyl acrylate (a2), above-mentioned rubber-like particle is formed by the segmented copolymer (b) of styrene butadiene, by improving the molecular resin amount that forms matrix, to adjust in the specific scope as the content of butadiene polymer structure in the particle size range of gluey particle and the said composition, obtained the good transparency, simultaneously also greatly improve shock-resistance and inflexible balance, and so far finished the present invention.
Promptly, impact-resistant transparent styron composition of the present invention, be by matrix and be dispersed in the impact-resistant transparent styron composition that the rubber-like particle in this matrix forms, it is characterized in that, above-mentioned matrix is formed by the multipolymer (A) of styrenic monomers (a1) and (methyl) alkyl acrylate (a2), and above-mentioned rubber-like particle is formed by the segmented copolymer (b) of styrene butadiene.
The Z molecular-weight average M of above-mentioned multipolymer (A)
zBe 22 * 10
4～28 * 10
4, the median size of above-mentioned rubber-like particle is 0.3～2.0 μ m, and the content of butadiene polymer structure is 2.0～7.5 quality % in the said composition.
Description of drawings
Fig. 1 is the process picture sheet that continuous block polymerization pipeline one example of the tubular reactor with static mixing component has been assembled in expression.Wherein, each symbol implication is as follows: the tubular reactor (10) that the tubular reactor (9) that tubular reactor (7) toothed gear pump (8) that the tubular reactor (6) that the tubular reactor (5) that (1) ram pump (2) stirring reactor (3) toothed gear pump (4) has a static mixing element has a static mixing element has a static mixing element has a static mixing element has a static mixing element has the acyclic polymerization pipeline of tubular reactor (I) circulating polymerization pipeline (II) of static mixing element
The working of an invention form
Transparent styrene resin composite of the present invention, as mentioned above, matrix is made of the multipolymer (A) of styrenic monomers (a1) and (methyl) alkyl acrylate (a2), and the rubber-like particle is made of the segmented copolymer (b) of styrene butadiene.
That is, multipolymer (A) forms the external phase in the composition, and the rubber-like particle exists with disperse phase.The rubber-like particle is the particle that is formed by styrene butadiene block copolymer (b).Specifically, consider from dispersed, shock-resistance aspect, at this particle surface,, preferably has the graft copolymerization part of styrenic monomers (a1) and (methyl) alkyl acrylate (a2) with respect to the allyl group that is present in the styrene butadiene block copolymer (b).At this moment, be linear structure in the styrenic monomers (a1) of this graft copolymerization part of the particle surface of rubber-like dispersed particle and the multipolymer of (methyl) alkyl acrylate (a2), exist with the matrix complexing.
In the present invention, because matrix is with the multipolymer (A) of styrenic monomers (a1) and (methyl) alkyl acrylate (a2) formation, so can pay the moulding product with the good transparency and rigidity.Among the present invention, be Z molecular-weight average M with multipolymer (A)
zBe taken as 22 * 10
4～28 * 10
4Be feature.This molecular weight ranges in the technical field of so-called styrene-propene acid alkyl ester multipolymer as the impact-resistant transparent styron composition of matrix, is the high molecular scope of having no precedent.By with the molecular weight of this multipolymer (A) as the high molecular zone, greatly improved the rigidity of moulding product.
On the other hand, the median size that is dispersed in the particle shape part of the styrene butadiene block copolymer (b) in this matrix is 0.3～2.0 μ m, and median size is taken as in this scope, can see that these moulding product have good shock-resistance.
And then, composition of the present invention, the content of the butadiene polymer structure in composition is the scope of 2.0～7.5 quality %.This scope is a low area as impact-resistant transparent styron composition, by possessing this numerical range, can greatly improve the rigidity of moulding product.The present invention has had both rigidity and shock-resistance, although fewer as the butadiene polymer structural content of rubber constituent, has embodied good shock-resistance, and this point is a bit that should point out especially.
That is, composition of the present invention by having both this all conditions, as thin slice moulding product, can have simultaneously and fail the transparency, shock-resistance and the rigidity that realize up till now.
The good especially this point of balance with regard to this performance sees, in the composition of the present invention, and the Z molecular-weight average M of multipolymer (A)
zBe preferably 22 * 10
4～28 * 10
4, the median size of rubber-like particle is preferably 0.3～1.0 μ m, and the polymer blocks content of divinyl is preferably 2.0～7.5 quality % in said composition.
The polymer blocks content of divinyl in the so-called herein composition is the peak-to-peak relative intensity according to the peak of measuring the polystyrene generation with IR and polyhutadiene generation, the quality criteria content that calculates.
Composition of the present invention had both had good shock-resistance, can greatly improve the rigidity of moulding product again, and the result can have both rigidity and shock-resistance.See with regard to the more remarkable this point of this effect, in the composition, the swelling index that is caused by 25 ℃ toluene in the rubber-like particle is 8～19, and total composition is preferably 0.2～0.8 at 25 ℃ toluene insoluble component content and the ratio of above-mentioned swelling index (toluene insoluble component content/swelling index).
The toluene insoluble component content of saying among the present invention and by the swelling index that toluene causes is measured in the following manner.
[the swelling index measuring method that toluene insoluble component content and toluene cause]
Precision takes by weighing the 1g rubber-modified copolymer resin, is that dissolving moved into lysate in the centrifuge tube after 24 hours in 25 ℃ of 100ml toluene, below 10 ℃, with 8500rpm centrifugation 15 minutes, utilize decant to remove supernatant liquor after, measure insoluble composition weight by toluene swell.Then, measure the weight of the toluene insoluble composition that obtains, utilize following formula to calculate toluene insoluble component content (%) 60 ℃ vacuum drier inner drying 24 hours.
Toluene insoluble component content (%)=(weight of toluene insoluble composition)/(weight of resin) * 100
Swelling index is calculated as follows.
Swelling index=(swollen toluene insoluble composition weight)/(dried toluene insoluble composition weight)
Graft copolymerization styrenic monomers (a1) partly as the particle surface that constitutes multipolymer (A) or rubber-like particle, vinylbenzene is for example arranged, alpha-methyl styrene, o-vinyl toluene, m-vinyl toluene, p-vinyl toluene, ethyl styrene, isobutyl-benzene ethene, t-butylstyrene, o-bromstyrol, m-bromstyrol, p-bromstyrol, o-chloro-styrene, m-chloro-styrene, p-chloro-styrene etc.In these, good from reactivity, be easy to reason considerations such as polymerization, preferably vinylbenzene.
Graft copolymerization (methyl) alkyl acrylate (a2) partly as the particle surface that constitutes multipolymer (A) or rubber-like particle, alkyl methacrylates such as methyl methacrylate, Jia Jibingxisuanyizhi, propyl methacrylate, butyl methacrylate are for example arranged, esters of acrylic acids such as methyl acrylate, ethyl propenoate, propyl acrylate, butyl acrylate, 2-ethylhexyl acrylate.In these, just improve the more broad aspect consideration of moulding product inflexible effect, preferably methyl methacrylate.The transparency and shock-resistance aspect with regard to the moulding product are considered, during polymerization, preferably also with methyl methacrylate and butyl acrylate.
Multipolymer (A) preferably contains styrol structural unit to form 30～60% ratio.That is, in the scope more than 30%, mobile fine during the composition fusion, formability is also very good, is taken as 60% when following, says that relatively the acrylic component amount that is caused by (a2) can improve, and the rigidity of moulding product, chemical-resistant can become better.
Multipolymer (A) is though contain Z molecular-weight average M
zBe 20 * 10
4～22.5 * 10
4Composition (following note do " composition (A1) ") and Z molecular-weight average M
zBe 23 * 10
4～29 * 10
4Composition (following note do " composition (A2) "), but consider from the rigidity aspect of thin slice moulding product, particularly from the balance aspect consideration of shock-resistance, composition (A1) is Z molecular-weight average M preferably
zBe 20 * 10
4～21.8 * 10
4Scope, and composition (A2) is Z molecular-weight average M preferably
zBe 23.5 * 10
4～29 * 10
4
The existence ratio of composition (A1) and composition (A2) is considered from improving rigidity effect aspect, is benchmark with the quality, preferably the ratio of (A1)/(A2)=85/15～30/70.
Consider that from the transparent aspect of thin slice moulding product styrol structural unit content in the styrol structural unit content of composition (A1) and the composition (A2) considers that from the rigidity and the shock-resistance aspect of moulding product any one is preferably 30～60% ratio.Consider from transparent aspect, with respect to styrol structural unit content in the composition (A1), preferably 0.8～1.2 times of the styrol structural unit content of composition (A2).
Constituting rubber-like segmented copolymer particle, styrene butadiene (b) is the multipolymer of styrenic monomers and diene monomer, as styrenic monomers, has as the cited various monomers of above-mentioned styrenic monomers (a1).Styrene monomer preferably.As diene monomer, divinyl, chloroprene, isoprene, 1,3-pentadiene etc. are arranged, from considering with the reactive good aspect of styrenic monomers, divinyl preferably.
The content of styrol structural unit in the styrene butadiene block copolymer (b) is considered from the balance aspect of the impact strength and the transparency, is preferably 33～55%.In the time of in the scope below 55%, butadiene block content can improve relatively, can obtain the moulding product of excellent impact resistance.In the time of in the scope more than 33%, improve the melt fluidity of styrene butadiene block copolymer (b), be easier to adjust with the viscosity of matrix, flowability during the composition fusion and the stable on heating balance of moulding product can become very good.
Above-mentioned styrene butadiene block copolymer (b), and then, close 1 in the key based on the insatiable hunger of divinyl, the ratio of 2-vinyl bonds is 14～35%, in order to improve shock strength, the preferably percentage of grafting in styrenic monomers (a1) and (methyl) alkyl acrylate (a2) and the graft copolymerization partly and the crosslinking degree of rubber-like particle on the equilibrium particle surface well.At this moment, 1, the nubbin of 2-vinyl bonds can form cis and trans key.
Consider from transparent aspect, contain styrol structural unit and be advisable to form 30～60% ratio in the multipolymer (A), and styrol structural unit content is preferably 33～55% in the styrene butadiene block copolymer (b).
The median size of rubber-like particle is 0.3～2.0 μ m, is preferably 0.4～1.0 μ m that this median size is to utilize the measured value of laser diffraction and scattering formula size-grade distribution meter (the hole field makes made LA-910) as median particle diameter.
Though the form of rubber-like particle does not have particular determination, consider from the shock-resistance aspect, preferably any in core shell structure, onion (onion) structure, sausage type (the サ ラ ミ) structure.Wherein, consider preferably have the onion structure from the shock-resistance aspect.
This impact-resistant transparent styron composition, with above-mentioned the same, have good shock-resistance and rigidity, specifically, as shock-resistance, with Du Pont's shock strength of the thick thin slice of 0.4mm more than 0.50J, as rigidity, according to the crooked elastic rate of the standard of JIS K7203 more than 2600MPa.
Impact-resistant transparent styron composition described above, its manufacture method is regulation not, can adopt intermittence type polymerization method, continous way polymerization etc. to make, and considers from being easy to make, be easy to adjust the rerum natura aspect, preferably according to following method manufacturing.
That is,, following method is arranged, styrenic monomers (a1), (methyl) alkyl acrylate (a2) and styrene butadiene block copolymer (b) are carried out the operation (operation 1) that polymerization obtains composition as concrete manufacture method, then,
With Z molecular-weight average M
zBe 23 * 10
4～29 * 10
4Styrenic monomers (a1) and the multipolymer of (methyl) alkyl acrylate (a2) (following this multipolymer note is made " multipolymer (A2) ") carry out blended operation (operation 2).
In this manufacture method, the composition that obtains in the operation 1 is to be formed by matrix and the rubber-like particle that is dispersed in this matrix, and this matrix is by Z molecular-weight average M
zBe 20 * 10
4～22.5 * 10
4The styrenic monomers (a1) and the multipolymer of (methyl) alkyl acrylate (a2) constitute (following this multipolymer note is made " multipolymer (A1) "), the rubber-like particle is to be made of styrene butadiene block copolymer (b).
Multipolymer (A1) and multipolymer (A2) are mixed formation above-mentioned multipolymer (A).That is, multipolymer (A1) is equivalent to the composition (A1) in the multipolymer (A), and multipolymer (A2) is equivalent to the composition (A2) in the multipolymer (A).
Operation 1 is with styrenic monomers (a1), (methyl) alkyl acrylate (a2), styrene butadiene block copolymer (b) and other can carry out the monomer of copolymerization as required, by block-suspension polymerization, solution polymerization or block polymerization, carry out the operation of graft copolymerization.
Herein, the ratio of styrenic monomers (a1), (methyl) alkyl acrylate (a2) and the styrene butadiene block copolymer (b) that uses, from the rigidity of moulding product, the transparency, and during the present composition fusion that finally obtains the good aspect of flowability consider, the mass ratio of styrenic monomers (a1) and (methyl) alkyl acrylate (a2) (a1)/(a2) is preferably 30/70～60/40 scope.When the usage rate of styrene butadiene block copolymer (b) was too small, the rubber-like particle formed granular, does not have shock-resistance.In order to embody shock-resistance, the rubber-like particle should have the particle diameter of appropriateness, the rubber-like particle preferably can form the particle diameter of core shell structure, onion structure, sausage type structure, for this reason, the usage quantity of styrene butadiene block copolymer (b), in material composition, the ratio of 7～18 quality % preferably.In the composition that finally obtains, with above-mentioned the same, consider from the shock-resistance aspect, preferably increase the particle diameter of dispersed particle, on the other hand, consider from the rigidity aspect, preferably reduce the amount of rubber-like particle, and improve the molecular weight of matrix.Consider from obtaining these performance balance aspects, in operation 1, the consumption of styrene butadiene block copolymer (b), the ratio of 10～14 quality % preferably in material composition.
(methyl) acrylate (a2) is by methyl methacrylate and (methyl) when butyl acrylate forms, (methyl) butyl acrylate is the scope of 1～5 quality % in (methyl) acrylate (a2), from the thermotolerance aspect of improving effect and moulding product of the transparency, shock-resistance, ideal.
As the concrete grammar of graft copolymerization, from production efficiency and production cost aspect and the consideration of composition excellent in uniform aspect, preferably continuous block polymerization method.
This continuous block polymerization method is to use several not movable mixing components partly is fixed on the continuous block polymerization pipeline that inner tubular reactor carries out several connections, the method that above-mentioned each material composition is carried out continuous block polymerization, from making the rubber-like particle form good dispersiveness and can evenly, easily increasing particle diameter and realize appropriate percentage of grafting aspect, ideal.Preferably, after the stirring reactor polymerization more than 1, import again in the above-mentioned continuous block polymerization pipeline and carry out continuous block polymerization after each material composition dissolving.
Here, use is fixed on inner tubular reactor with stirring reactor and mixing component with several no moving parts and carries out the successive polymerization pipeline that several continuous block polymerization pipelines that are connected connect and see best from production efficiency, as this successive polymerization pipeline, for example preferably by the polymerization pipeline that constitutes with the lower section shown in Figure 1, promptly, a, stirring reactor, b, be connected with stirring reactor, several do not have the initial stage polymerization pipeline that the tubular reactor of the mixing component of moving part forms fully by 1 above internal fixation, c, be connected with initial stage polymerization pipeline, the main polymerization pipeline that forms by the tubular reactor of 1 several static part mixing component of above internal fixation, d, between polymerization pipeline and the main polymerization pipeline, return the reflux pipeline of initial stage polymerization pipeline as branch line in the early stage.
As mixing component used herein, the shunting of the polymer fluid stream in the inflow pipe that for example changes and the flow direction and by shunting repeatedly and the interflow makes polymer fluid carry out blended.As such tubular reactor, the ス Le ザ-Shi tubular mixer of SMX type, SMQ type, the static mixer of ケ ニ Star Network ス formula, the tubular mixer of eastern レ formula etc. are for example arranged.
Following operation 1 polymerization process that uses this continuous block polymerization pipeline according to the process picture sheet explanation of Fig. 1.
Utilize ram pump (1) that material composition is at first sent in the stirring reactor (2), after carrying out the initial stage graft polymerization under stirring, in tubular reactor (4), (5 of using toothed gear pump (3) to send into again to have static mixing component) and (6) and the circulating polymerization pipeline (I) with toothed gear pump (7).
Initial stage graft polymerization at stirring reactor (2), the total polymerisation conversion of styrenic monomers (a1) and (methyl) alkyl acrylate (a2), exit in reactor (2), preferably according to 10～28 weight %, better 14～24 weight % implement.As stirring reactor (2), stirring-type tank reactor, stirring-type tower reactor etc. are for example arranged, as paddle, for example, the paddle of anchor type, Scroll-type, spiral type, diclinic gear type etc. is arranged.
Then, in circulating polymerization pipeline (I), polymerization is carried out on circulation limit, polymer fluid limit, and wherein a part of polymer fluid is sent into down together in the acyclic polymerization pipeline (II).Polymer fluid flow at circulating polymerization pipeline (I) internal recycle is called reflux ratio with the ratio that flows into the polymer fluid flow in the acyclic polymerization pipeline (II), in will not flowing into acyclic polymerization pipeline (II), and be taken as F1 (rise/hour) at the mixed solution flow of circulating polymerization pipeline (I) internal reflux, will be when circulating polymerization pipeline (I) flow into mixed solution flow the acyclic polymerization pipeline (II) and be taken as F2 (rise/hour), R=F1/F2 is preferably 3～15 usually.
Graft polymerization in this circulating polymerization pipeline (I), the total polymerisation conversion of this circulating polymerization pipeline (I) exit styrenic monomers (a1) and (methyl) alkyl acrylate (a2), usually by 35～55 quality %, best 40～50 quality % carry out polymerization.As polymerization temperature, be advisable for 120～135 ℃.
Polymerization temperature in acyclic polymerization pipeline (II) is generally 140～160 ℃, carries out graft polymerization continuously, till the polymerisation conversion that reaches 60～85 quality %.
Then, utilize toothed gear pump (11) that this mixed solution has been sent into preheater, then send into the devolatilization groove, under reduced pressure remove unreacted monomer and solvent after, obtain desired composition by granulating.
In operation 1, in order to reduce the viscosity of above-mentioned mixed solution in the reactor, can use solvent, its consumption is 5～20 mass parts with respect to the starting monomer that adds up to 100 mass parts.As solvent types, use the toluene that uses in the block polymerization method, ethylbenzene, dimethylbenzene etc. usually.
In operation 1, adjust to optimum range for the particle dia of dispersate in the composition that will obtain, in order to regulate the molecular weight of matrix, preferably add chain-transfer agent.The addition of this chain-transfer agent with respect to the starting monomer that adds up to 100 weight parts, is 0.005～0.5 weight part.
In the polymerization of operation 1, can suitably use polymerization starter, the example as polymerization starter has 1, two (t-butyl peroxy) hexanaphthenes, 1 of 1-, two (the t-butyl peroxy) 3,3 of 1-, 5-trimethyl-cyclohexane, 2, two (t-butyl peroxy) butane of 2-, n-butyl-4, two (t-butyl peroxy) valerates of 4-, t-butyl peroxy acetic ester, t-butyl peroxy-3,3,5-tri-methyl hexanoic acid ester, t-butyl peroxy laurate, t-butyl peroxy benzoic ether.
Two (t-butyl peroxy) isophthalic acid ester, 2; 5-dimethyl-2, two (the benzyl acyl group peroxide) hexanes of 5-, t-butyl peroxy toxilic acid, t-butyl peroxy sec.-propyl monocarbonate, two-t-butylperoxide, dicumyl peroxide, t-butyl hydroperoxide, cumene hydroperoxide etc.
The composition that obtains like this, matrix are to be formed by the multipolymer of composition (A1) (A), and the rubber-like particle that is dispersed in this matrix is to be formed by above-mentioned styrene butadiene block copolymer (b).
The composition fusion flow velocity that obtains in the operation 1 does not have particular determination, but the fusion flow velocity is crossed when hanging down, the processing forming variation of final desired impact-resistant transparent styron composition, when too high, be easy to drawdown (draw down), so according to the standard of JIS K7210, at 200 ℃, when the 5kgf loading was measured the fusion flow velocity down, this fusion flow velocity (MFR) was preferably 1～10g/10 minute.From the drawdown consideration, more preferably 1～2.5g/10 minute.
Then, operation 2 is mixed copolymer in the composition that obtains in operation 1 (A2).
Among the present invention, have with operation 1 in the equal monomer of the composition mesostroma that obtains form, and by mixing the high-molecular weight multipolymer, when particularly being processed into thin slice moulding product, except greatly improving its rigidity, the transparency of moulding product is also fairly good.
Multipolymer used herein (A2), styrol structural unit content is preferably 0.8～1.2 times for multipolymer (A1).By being taken as this scope, it is fabulous that the transparency of moulding product also becomes.
During multipolymer (A2) polymerization, as (methyl) acrylate (b2), also with methyl methacrylate and (methyl) butyl acrylate the time, in (methyl) acrylate (b2), (methyl) butyl acrylate is the scope of 1～5 quality %, the flowability during from the composition fusion and prevent that sheet moulding product drawdown aspect is ideal.
This multipolymer (A2) also can pass through block one suspension polymerization, solution polymerization or block polymerization, makes styrenic monomers (a1) and (methyl) alkyl acrylate (a2) carry out graft copolymerization.When carrying out this polymerization, can in polymer raw, add organic solvent as required.As organic solvent, ethyl benzene,toluene,xylene, acetone, isopropyl benzene, methyl ethyl ketone, hexane etc. are arranged, preferably use ethylbenzene, toluene.
In operation 2, as making composition and multipolymer (A2) the blended method that obtains in the operation 1, there is not particular determination, consider from the homogeneity aspect of composition, preferably utilize melt blending to carry out, specifically, have both heating and meltings are carried out the blended method.For example, with the composition that obtains in the operation 1 and the particle or the particulate of multipolymer (A2), carry out melt blending with forcing machine at 200～240 ℃, direct sheetization is in case after the granulating, also can carry out the fusion sheetization with forcing machine once more.
The multipolymer (A2) that uses in operation 2 can pass through block one suspension polymerization, and solution polymerization or block polymerization make styrenic monomers (a1) and (methyl) alkyl acrylate (a2) carry out graft copolymerization.When carrying out this polymerization, as required, can in polymer raw, add organic solvent.As organic solvent, ethyl benzene,toluene,xylene, acetone, isopropyl benzene, methyl ethyl ketone, hexane etc. are arranged, preferably use ethylbenzene, toluene.
The mixture ratio of composition that obtains in the operation 1 and multipolymer (A2), for example, in quality criteria, said composition/multipolymer (A2)=50/50～90/10 preferably.But the content at polybutadiene configuration position in the present composition that finally obtains than converting, is necessary for 2.0～7.5 quality % with raw materials quality during mixing.
In the present invention, during the polymerization of operation 1, and during the manufacturing of multipolymer (A2) or the fusion of operation 2 when mixing, as required, can mix the various additives that generally can add in the phenylethylene resin series, releasing agent for example, UV light absorber, tinting material, oxidation inhibitor, thermo-stabilizer, softening agent, dyestuff etc.Can be when mixing, or add in the polymerization of each polymkeric substance, without any problem.
Specifically, it is that softening agent, polyester are metal-salt, silicone oil of softening agent such as softening agent, oxidation inhibitor, chain-transfer agent, higher fatty acid, high-grade aliphatic ester, higher fatty acid etc. that mineral oil, ester are arranged, being used in combination more than a kind or 2 kinds in these.
The impact-resistant transparent styron composition of the present invention that so obtains as previously mentioned, as sheet moulding product, aspect the transparency, shock-resistance, rigidity, has been got the excellent results of having no precedent.As the transparency, for example according to the standard of ASTM D1003, the turbidity that uses 2mm test injection sheet is below 10.
Impact-resistant transparent styron composition of the present invention, the sheet extrusion moulding is very good, and shock-resistance and inflexible balance are also fabulous, at sheet moulding product, for example used for packing foods dish, lid material, box, various splendid attire are with extremely useful in the purposes such as dish, travelling belt.
Impact-resistant transparent styron composition of the present invention, except sheet moulding product purposes, because have both rigidity, shock-resistance, the transparency, and then because the so-called special property that is rich in formability, so also applicable to injection molding, single shaft extrusion moulding, in the various moulding purposes such as biaxial stretch-formed extrusion moulding, blowing extrusion molding, roll moulding, special-shaped extrusion moulding, vacuum forming, the empty moulding of pressure, also can be used as the various parts, FOLD AND PACK, stationery, sundry goods of the housing of tame electrical article and part, OA equipment etc.
Embodiment
Physics value in the example is measured as follows.
(1) turbidity of plate
According to ASTM D1003 standard, use the thick test injection sheet of 2mm to measure.
(2) Du Pont's shock strength
Use Du Pont's shock-testing machine (the smart mechanism of Japan is done made), obtain 50% failure energy (weight 200g clashes into the radius 6.3mm of core end, bears the radius 6.3mm of table top) of 0.4mm slab-like test film.
(3) crooked elastic rate
According to the standard of JIS K7203, trial speed is taken as 2mm/ minute, ask its value.
(4) MFR (fusion flow velocity)
Press the standard of JIS K7210, under 200 ℃, 5kgf loading, measure.
(5) drawdown evaluation
Using sheet extruder (screw diameter 30mm), is 210 ℃～230 ℃, extruded velocity 0.8-1m/ minute with molten resin temperature, to the resin particle extruding, is made into the thick sheet sample of 0.4mm.Then, use vacuum forming machine, after this sheet sample is heated with 290～300 ℃ Heating temperature, 10 seconds～30 seconds heat-up time, unilateral as benchmark with before the sheet heating measured the sagging length of sheet middle body, with respect to heat-up time, according to the sagging length of sheet, estimate drawdown.
During 20 seconds heat-up times, sag of chain is lower than that 40mm is zero, 40mm above for *.
During 30 seconds heat-up times, sag of chain is lower than that 60mm is zero, 60mm above for *.
The Production Example of composition (operation 1)
The manufacturing of composition (1)
50 parts of vinylbenzene, 45 parts of methyl methacrylates (MMA) and 5 parts of butyl acrylates (BuA), 10 parts of ethylbenzenes, 14 parts of styrene butadiene block copolymers (styrene monomer unit content 40%) are made mixing solutions, as polymerization starter, with respect to 100 parts of monomer mixtures, add 0.02 part of t-butyl peroxy benzoic ether; As chain-transfer agent, with respect to 100 parts of monomer mixtures, add 0.1 part of n-lauryl mercaptan, use the polymerization pipeline shown in Fig. 1 process picture sheet, carry out continuous block polymerization under the following conditions.
Temperature of reaction in the stirring reactor (2): 120 ℃
Temperature of reaction in the circulating polymerization pipeline (I): 140 ℃
Temperature of reaction in the acyclic polymerization pipeline (II): 150 ℃
The mixing solutions that polymerization is obtained is with heat exchanger heats to 225 ℃, remove volatile component under the decompression after, granulating obtains composition (1).The rerum natura of resulting composition is shown in table 1.
The manufacturing of composition (2)
In the mixed solution that forms by 50 parts of vinylbenzene, 45 parts of methyl methacrylates (MMA) and 5 parts of butyl acrylates (BuA), 9 parts of ethylbenzenes, 11 parts of styrene butadiene block copolymers (styrene monomer unit content 40%), as polymerization starter, add 0.02 part of t-butylbenzene manthanoate with respect to 100 parts of monomer mixtures; As chain-transfer agent, add 0.1 part of n-lauryl mercaptan with respect to 100 parts of monomer mixtures, in addition, with the same composition (2) that obtains of Production Example of composition (I).The rerum natura of resulting composition is shown in table 1.
The preparation of multipolymer (A2)
The preparation of multipolymer (A2-1)
Make to mix and hold liquid by 50 parts of vinylbenzene, 47.5 parts of methyl methacrylates (MMA) and 2.5 parts of butyl acrylates (BuA), 8 parts of ethylbenzenes,,, add 0.02 part of t-butyl peroxy benzoic ether with respect to 100 parts of monomer mixtures as polymerization starter; As chain-transfer agent, with respect to 100 parts of monomer mixtures, add 0.1 part of n-lauryl mercaptan, under the following conditions, carry out block polymerization continuously.
Temperature of reaction in the stirring reactor (2): 120 ℃
Temperature of reaction in the circulating polymerization pipeline (I): 140 ℃
Temperature of reaction in the acyclic polymerization pipeline (II): 150 ℃
The mixing solutions that polymerization is obtained is with heat exchanger heats to 225 ℃, remove volatile component under the decompression after, carry out granulating, obtain copolymer resin (A2-1).The multipolymer rerum natura that obtains is shown in table 2.
The manufacturing of multipolymer (A2-2)
Make mixing solutions by 50 parts of vinylbenzene, 47.5 parts of methyl methacrylates (MMA) and 2.5 parts of butyl acrylates (BuA), 8 parts of ethylbenzenes,,, add 0.02 part of t-butyl peroxy benzoic ether with respect to 100 parts of monomer mixtures as polymerization starter; As chain-transfer agent, with respect to 100 parts of monomer mixtures, add 0.09 part of n-lauryl mercaptan, in addition, with the same multipolymer (A2-2) that obtains of Production Example of multipolymer (A2-1), the rerum natura of gained multipolymer is shown in table 2.
The manufacturing of multipolymer (A2-3)
Make mixing solutions by 50 parts of vinylbenzene, 47.5 parts of methyl methacrylates (MMA) and 2.5 parts of butyl acrylates (BuA), 8 parts of ethylbenzenes,,, add 0.02 part of t-butyl peroxy benzoic ether with respect to 100 parts of monomer mixtures as polymerization starter; As chain-transfer agent, with respect to 100 parts of monomer mixtures, add 0.12 part of n-lauryl mercaptan, in addition, with the same multipolymer (A2-3) that obtains of Production Example of multipolymer (A2-1).The rerum natura of gained multipolymer is shown in table 2.
Embodiment 1
Cooperation ratio by 70/30 in composition (1) adds multipolymer (A2-1), and the thick thin slice of 0.4mm is made in extrusion moulding, utilizes injection molding to be made into JIS test film and the thick sheet moulding product of 2mm, and with the various rerum naturas of these sample determinations, measured value is shown in table 3.Sheet condition of molding and injection molding condition are as follows.
Sheet forming machine: the system UEV of ユ ニ オ Application プ ラ ス チ Star Network Co., Ltd. type 30mm forcing machine
Barrel temperature: 220 ℃, T mould design temperature: 220 ℃
Injection moulding machine: the system SAV-30-30-P of the smart machine in mountain city Co., Ltd. injection moulding machine.
Barrel temperature: 230 ℃, die temperature: 50 ℃
Embodiment 2
Add multipolymer (A2-2) by 60/40 cooperation ratio in composition (1), under the condition identical with embodiment 1, make thick thin slice of 0.4mm and test injection sheet, measure various rerum naturas, measured value is shown in table 3.
Embodiment 3
Add multipolymer (A2-3) by 60/40 cooperation ratio in composition (1), under the condition identical with embodiment 1, make thick thin slice of 0.4mm and test injection sheet, measure various rerum naturas, measured value is shown in table 3.
Comparative example 1
Under the condition identical with embodiment 1, composition (1) monomer is made thick sheet of 0.4mm and test injection sheet, measure various rerum naturas, measured value is shown in table 4.
Comparative example 2
Under the condition identical with embodiment 1, composition (2) monomer is made thick sheet of 0.4mm and test injection sheet, measure various rerum naturas, measured value is shown in table 4.
Comparative example 3
Add multipolymer (II-2) by 20/80 cooperation ratio in composition (1), under the condition identical with embodiment 1, make thick thin slice of 0.4mm and test injection sheet, measure various rerum naturas, measured value is shown in table 4.[table 1]
| Composition | ????1 | ????2 | |
| (A) vinylbenzene (part) | ????50 | ????50 | |
| (B) | MMA (part) | ????45 | ????45 |
| BuA (part) | ????5 | ????5 | |
| (C) rubber (part) | ????14 | ????11 | |
| Dispersion rubber particle diameter (μ m) | ????0.5 | ????0.22 | |
| M z×10 4 | ????21.4 | ????21.6 | |
| The plate turbidity | ????3.5 | ????3.0 | |
| MFR (g/10 branch) | ????2.5 | ????2.1 | |
[table 2]
[table 3]
[table 4]
| Multipolymer | A2-1 | ?A2-2 | ?A2-3 | |
| (A ') vinylbenzene (part) | 50 | ?50 | ?50 | |
| (B’) | MMA (part) | 47.5 | ?47.5 | ?50 |
| BuA (part) | 2.5 | ?2.5 | ?0 | |
| M z×10 4 | 24.2 | ?26.0 | ?24.5 | |
| The plate turbidity | 0.4 | ?0.4 | ?0.4 | |
| MFR (g/10 branch) | 2.1 | ?1.9 | ?1.2 | |
| Embodiment | 1 | ?2 | ?3 |
| Composition (1) | 60 | ?60 | ?60 |
| Composition (2) | |||
| Copolymer A 2-1 | 40 | ||
| Copolymer A 2-2 | ?40 | ||
| Copolymer A 2-3 | ?40 | ||
| The plate turbidity | 2.0 | ?2.0 | ?2.5 |
| Du Pont's shock strength (J) | 0.51 | ?0.55 | ?0.62 |
| Crooked elastic rate (MPa) | 2750 | ?2770 | ?2800 |
| Drawdown | ○ | ?○ | ?○ |
| The toluene insoluble component content | 6.7 | ?6.7 | ?6.7 |
| Swelling index | 14 | ?14 | ?14 |
| Insoluble composition/swelling index butadiene content M z×10 4 | 0.5 6 22.5 | ?0.5 ?6 ?22.8 | ?0.5 ?6 ?22.5 |
| Comparative example | 1 | ?2 | ?3 |
| Composition (1) | 100 | ?20 | |
| Composition (2) | ?100 | ||
| Copolymer A 2-1 | |||
| Copolymer A 2-2 | ?80 | ||
| The plate turbidity | 3.5 | ?3.0 | ?0.9 |
| Du Pont's shock strength (J) | 1.00 | ?0.40 | ?0.08 |
| Crooked elastic rate (MPa) | 2430 | ?2500 | ?2870 |
| Drawdown | ○ | ?○ | ?○ |
| The toluene insoluble component content | 11.1 | ?9.0 | ?2.3 |
| Swelling index | 14 | ?14 | ?9 |
| Insoluble composition/swelling index butadiene content M z×10 4 | 0.8 8 21.4 | ?0.7 ?7 ?21.6 | ?0.3 ?1.5 ?24.8 |
Good transparent styron composition of a kind of transparency, shock-resistance and rigidity and manufacture method thereof can be provided according to the present invention.
In sheet moulding product, can prevent from moulding product top isolating of increasing the weight of to cause or be out of shape, because the transparency is good, so the visuality of content is also very good.Therefore, extremely useful in purposes such as used for packing foods dish, lid material, box, various splendid attire dish, travelling belt.
Claims (6)
1. impact-resistant transparent styron composition, form by matrix and the rubber-like particle that is dispersed in this matrix, it is characterized in that, above-mentioned matrix is made of the multipolymer (A) of styrenic monomers (a1) and (methyl) alkyl acrylate (a2), above-mentioned rubber-like particle is made of styrene butadiene block copolymer (b), the Z-average molecular weight M of above-mentioned multipolymer (A)
zBe 22 * 10
4～28 * 10
4, the median size of above-mentioned rubber-like particle is 0.3～2.0 μ m, and the content of butadiene polymer block is 2.0～7.5 quality % in the said composition.
2. according to the composition of claim 1 record, wherein, the rubber-like particle in 25 ℃ toluene swelling index be 8～19, and total composition is 0.2～0.8 at the content of 25 ℃ toluene insoluble composition with the ratio of above-mentioned swelling index (toluene insoluble component content/swelling index).
3. according to the composition of claim 2 record, it is characterized in that the content of styrol structural unit is 30～60% in the above-mentioned multipolymer (A), and the content of styrol structural unit is 33～55% in the styrene butadiene block copolymer (b).
4. according to the composition of claim 1 or 3 records, it is characterized in that above-mentioned (methyl) alkyl acrylate (a2) is made of (methyl) methyl acrylate and (methyl) butyl acrylate.
5. according to the composition of claim 1 record, it is characterized in that above-mentioned multipolymer (A) is by Z-average molecular weight M
zBe 20 * 10
4～22.5 * 10
4Composition and Z-average molecular weight M
zBe 23 * 10
4～29 * 10
4One-tenth be grouped into.
6. according to the composition of claim 5 record, it is characterized in that, contain Z-average molecular weight M
zBe 20 * 10
4～22.5 * 10
4Composition and Z-average molecular weight M
zBe 23 * 10
4～29 * 10
4Composition, in quality criteria, the former/latter=85/15～30/70.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02120639 CN1210323C (en) | 2002-02-11 | 2002-02-11 | Impact-resistant transparent styron composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02120639 CN1210323C (en) | 2002-02-11 | 2002-02-11 | Impact-resistant transparent styron composition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1438267A true CN1438267A (en) | 2003-08-27 |
| CN1210323C CN1210323C (en) | 2005-07-13 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101550262B (en) * | 2008-03-31 | 2012-07-11 | 旭化成化学株式会社 | Optical forming body |
| CN108473697A (en) * | 2016-01-13 | 2018-08-31 | 电化株式会社 | Biaxial stretch-formed and its formed products |
-
2002
- 2002-02-11 CN CN 02120639 patent/CN1210323C/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101550262B (en) * | 2008-03-31 | 2012-07-11 | 旭化成化学株式会社 | Optical forming body |
| CN108473697A (en) * | 2016-01-13 | 2018-08-31 | 电化株式会社 | Biaxial stretch-formed and its formed products |
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| Publication number | Publication date |
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| CN1210323C (en) | 2005-07-13 |
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