WO2022100015A1 - 一种聚碳酸酯组合物及其制备方法和应用 - Google Patents
一种聚碳酸酯组合物及其制备方法和应用 Download PDFInfo
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- WO2022100015A1 WO2022100015A1 PCT/CN2021/089881 CN2021089881W WO2022100015A1 WO 2022100015 A1 WO2022100015 A1 WO 2022100015A1 CN 2021089881 W CN2021089881 W CN 2021089881W WO 2022100015 A1 WO2022100015 A1 WO 2022100015A1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/49—Phosphorus-containing compounds
- C08K5/51—Phosphorus bound to oxygen
- C08K5/52—Phosphorus bound to oxygen only
- C08K5/524—Esters of phosphorous acids, e.g. of H3PO3
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/15—Heterocyclic compounds having oxygen in the ring
- C08K5/151—Heterocyclic compounds having oxygen in the ring having one oxygen atom in the ring
- C08K5/1535—Five-membered rings
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2201/00—Properties
- C08L2201/02—Flame or fire retardant/resistant
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2201/00—Properties
- C08L2201/08—Stabilised against heat, light or radiation or oxydation
Definitions
- the present invention relates to the technical field of polymer materials, in particular to a polycarbonate composition and a preparation method and application thereof.
- PC Polycarbonate
- the prior art mainly improves the fluidity of the resin by adjusting the molecular weight and distribution of the resin, thereby improving the processability of the material.
- the polycarbonate obtained by this method will lead to a decline in mechanical properties such as impact, and the Disadvantages of greatly reduced stress cracking and poor solvent resistance.
- There are also studies to improve the processability of materials by adding low molecular weight oligomers to polycarbonate for example, US 2003/0181603, US 2009/0312479, WO 2011/014778 and US 2015/0183986 describe the use of low molecular weight polyhydrocarbon resins As a flow modifier a composition with good impact toughness, flowability and thermal deformation stability.
- WO 2017/005739 discloses diglycerides as flow modifiers, characterized by good mechanical properties, very good rheological properties (easy flow) and high thermal shape stability.
- the above-mentioned methods of adding low-molecular-weight substances may lead to a decrease in the heat resistance of the material.
- the relatively long residence time results in a large amount of color components, resulting in discoloration during processing and molding.
- the material will also be reduced. flame retardant properties.
- the existing technology mainly reduces the adhesion between the plastic and the metal mold by adding external lubricants, but it will increase the risk of precipitation and sticking, resulting in appearance defects in injection molding (instruction Figure 2), or affect the subsequent spraying or welding process.
- the core of the part is usually separated mechanically by means of an ejector pin.
- the demolding performance is poor, the ejection force of the mold is too large, and the ejector pin will whiten the part in light, and destroy the part in heavy; on the contrary, when the demolding force is too small, the part will easily slip off, which is not conducive to the operation of the robot in automation. Therefore, ensuring the proper mold release of the material is the key to ensuring normal production.
- An object of the present invention is to provide a polycarbonate composition with good moldability and good releasability.
- Another object of the present invention is to provide a method for preparing the above-mentioned polycarbonate composition.
- a polycarbonate composition in parts by weight, comprising 100 parts of polycarbonate resin, 0.15-1.5 parts of compound components; the compound components are hindered phenol aromatic derivatives, phosphoric acid quencher, Compounding of furanone derivatives, wherein, based on the total weight of the compounding components, hindered phenol aromatic derivatives accounts for 5-15wt%; phosphoric acid quencher accounts for 10-30wt%; furan The weight percentage of ketone derivatives is 55-85 wt%.
- the hindered phenol aromatic derivatives is selected from ⁇ -(4-hydroxy-3,5-di-tert-butylphenyl) propionic acid n-octadecyl ester, tetrakis[methyl-(3,5-di-tert-butyl) At least one of the group-4-hydroxyphenyl) propionate] pentaerythritol ester and triethylene glycol ether-bis(3-tert-butyl-4-hydroxy-methylphenyl) propionate.
- the hindered phenol arene derivatives are selected from triethylene glycol ether-bis(3-tert-butyl-4-hydroxy-methylphenyl)propionate.
- the phosphoric acid quencher is selected from tris(2,4-di-tert-butylphenyl) phosphite, dioctadecyl pentaerythritol bisphosphite, bis(2,4-di-tert-butyl) pentaerythritol diphosphite. at least one of phosphites.
- the phosphoric acid quencher is selected from bis(2,4-di-tert-butyl) pentaerythritol diphosphite.
- the furanone derivative is selected from xylyl dibutylbenzofuranone.
- the hindered phenol aromatic hydrocarbon derivatives account for 7-13wt%; the phosphoric acid quencher accounts for 15-25wt%; the furanone derivatives account for the weight% 62-78 wt%.
- the content is preferably, the amount of the compound component is 0.3-0.9 part.
- the addition amount of the compounding components reaches 0.3 parts, good demoldability and formability can be obtained, and when the addition amount reaches 0.9 parts, the demoulding force is not significantly improved.
- the demoulding force refers to the resistance that needs to be overcome when the plastic part is released from the core.
- the schematic diagram is shown in Figure 1 of the following specification.
- f is the friction coefficient between the core and the part
- A is the contact area between the core and the part
- the demolding force is characterized by measuring the force required to remove the cylinder on the core.
- the weight average molecular weight of polycarbonate resins suitable for injection molding processing is 19,000-35,000.
- the flame retardants are selected from C1-C16 alkyl sulfonate flame retardants, carbonate flame retardants, inorganic phosphate flame retardants, At least one of fluorine-silver ion complexes and phosphate ester flame retardants;
- the C1-C16 alkyl sulfonate flame retardants are selected from potassium perfluorooctane sulfonate, tetrafluoroethanesulfonate At least one of ethylammonium and potassium diphenylsulfone sulfonate;
- the carbonate flame retardant is selected from at least one of sodium carbonate, potassium carbonate, magnesium carbonate, calcium carbonate and barium carbonate.
- the preparation method of the above-mentioned polycarbonate composition includes the following steps: mixing the components uniformly, and then extruding and granulating through a twin-screw extruder to obtain the polycarbonate composition, wherein the temperature of the screw is 240° C. to 260° C. °C, the rotation speed is 400 ⁇ 600rpm.
- the present invention has the following beneficial effects:
- the present invention can not only obtain a good antioxidant effect by selecting the compound of hindered phenol aromatic derivatives, phosphoric acid quenchers and furanone derivatives. , and can replace the addition of lubricant, and reduce the mold release force, improve the injection molding process performance.
- the flame retardancy can be significantly improved.
- Figure 1 Schematic representation of demolding force.
- the raw materials used in the present invention are derived from commercially available products:
- Polycarbonate resin PC 1300 10NP, weight average molecular weight 22000.
- Hindered phenol aromatic derivatives A n-octadecyl ⁇ -(4-hydroxy-3,5-di-tert-butylphenyl) propionate;
- Hindered phenol aromatic hydrocarbon derivative B tetrakis[methyl-(3,5-di-tert-butyl-4-hydroxyphenyl)propionic acid]pentaerythritol ester.
- Hindered phenol aromatic derivative C triethylene glycol ether-bis(3-tert-butyl-4-hydroxy-methylphenyl)propionate.
- Phosphoric Acid Quencher A Tris(2,4-di-tert-butylphenyl)phosphite.
- Phosphoric Acid Quencher B Dioctadecyl pentaerythritol bisphosphite.
- Phosphoric acid quencher C bis(2,4-di-tert-butyl) pentaerythritol diphosphite.
- Furanone Derivatives Xylyldibutylbenzofuranone.
- Antioxidant A N,N'-bis-(3-(3,5-di-tert-butyl-4-hydroxyphenyl)propionyl)hexanediamine.
- Antioxidant B 1,3,5-tris(3,5-di-tert-butyl-4-hydroxyphenylpropionyloxyethyl)isocyanurate.
- Antioxidant C 3,9-bis[1,1-dimethyl-2-[(3-tert-butyl-4-hydroxy-5-methylphenyl)propionyloxy]ethyl]-2 ,4,8,10-Tetraoxaspiro[5.5]undecane.
- Antioxidant D 1,3,5-Tris(4-tert-butyl-3-hydroxy-2,6-dimethylbenzyl)-1,3,5-triazine-2,4,6-( 1H,3H,5H)-triketone.
- Lubricant A GLYCOLUBE-P, Lonza
- Lubricant B A-C6A, Honeywell;
- Lubricant C MB50-002, Dow Corning
- Examples and comparative examples The preparation method of the polycarbonate composition: Mix the components uniformly, and then extrude and granulate through a twin-screw extruder to obtain a polycarbonate composition, wherein the temperature of the screw is 240 °C ⁇ 260 °C , the speed is 400 ⁇ 600rpm.
- f is the friction coefficient between the core and the part
- Grade 1 No visible silver wires on the outside, no sink marks on the outside, and no holes on the inside;
- Level 2 A small amount of silver wire can be seen at the gate, no sink marks on the outside, and no holes on the inside;
- Level 3 A small amount of silver wire can be seen on the whole part, no sink marks on the outside, and no holes on the inside;
- Grade 4 A small amount of silver wire can be seen on the whole part, no sink marks can be seen on the outside, and the internal holes are less than 0.5cm;
- Grade 5 A small amount of silver wire can be seen on the whole part, no sink marks on the outside, and internal holes > 0.5cm.
- the flame height is 20 ⁇ 1mm
- the Bunsen burner is placed in the center of the sample
- the mouth of the Bunsen burner is 10 ⁇ 1mm away from the bottom of the sample
- the ignition time is 10 ⁇ 0.5s
- the speed is 300mm/s after 10 ⁇ 0.5s ignition.
- Table 1 Component content (parts by weight) and test results of the polycarbonate compositions of Examples 1-8
- the phosphoric acid quencher is preferably bis(2,4-di-tert-butyl) pentaerythritol diphosphite
- the hindered phenol aromatic hydrocarbon derivative is preferably triethylene glycol ether-bis(3-tert-butyl-) 4-Hydroxy-methylphenyl)propionate.
- Comparative Examples 12-14 It can be seen from Comparative Examples 12-14 that although commonly used lubricants are often used as mold release agents, they are insufficient in improving the formability of materials.
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Abstract
本发明公开了一种高可靠良成型聚碳酸酯组合物,按重量份计,包括100份聚碳酸酯树脂、0.15-1.5份的复配组分;所述的复配组分为受阻酚芳烃衍生物、磷酸猝灭剂、呋喃酮衍生物的复配,其中,以复配组分的总重量计,受阻酚芳烃衍生物所占重量百分比为5-15wt%;磷酸猝灭剂所占重量百分比为10-30wt%;呋喃酮衍生物所占重量百分比为55-85wt%。通过特定的复配组分,能够明显提升聚碳酸酯组合物的成型性、脱模性。当添加阻燃剂时,能够明显提升阻燃性。
Description
本发明涉及高分子材料技术领域,特别是涉及一种聚碳酸酯组合物及其制备方法和应用。
聚碳酸酯(PC)是性能优异的工程塑料,具有良好的综合性能,机械强度高、耐冲击韧性好、尺寸稳定、耐热较好、电绝缘性好,在家电,数码产品,IT产品等等领域具有广泛的应用。
为了得到良好的成型性,现有技术主要是通过树脂分子量及分布调整提升树脂流动性,从而提高材料的加工性能,但是由该方法得到的聚碳酸酯,会导致冲击等力学性能的下降,耐应力开裂性大幅度降低并且耐溶剂性差的缺点。也有研究通过在聚碳酸酯中添加低分子量低聚物来提高材料的加工性能,例如,US 2003/0181603、US 2009/0312479、WO 2011/014778和US 2015/0183986描述了通过低分子量聚烃树脂作为流动改性剂具有良好的冲击韧性,流动性和热变形稳定性的组合物。WO 2017/005739公开了双甘油酯作为流动改性剂,其特征在于良好的机械性能、非常好的流变性能(易流动)和高的加热形状稳定性。然而,上述的这些外加低分子物质的方法,可能导致材料耐热性下降,尤其是滞留时间相对较长是产生的显色成分多,导致加工成型变色,此外在阻燃体系,还会降低材料的阻燃性能。
另外,为了得到良好的脱模性,现有技术主要是通过添加外润滑剂,减少塑料与金属模具之间的粘结,但会增加析出发粘的风险,导致注塑成型中的外观缺陷(说明书附图2),或者影响后续喷涂或焊接加工。在注射成型出模阶段,通常是通过顶杆机械地使制件模芯分离。当脱模性差式,模具脱出力过大,顶杆轻则顶白制件,重则破坏制件;相反,当脱模力过小,制件易滑脱,不利于自动化中的机械手操作。因此,保证材料适当的脱模性是保证正常生产的关键。
发明内容
本发明的目的在于,提供一种具有良成型、脱模性好的聚碳酸酯组合物。
本发明的另一目的在于,提供上述聚碳酸酯组合物的制备方法。
本发明是通过以下技术方案实现的:
一种聚碳酸酯组合物,按重量份计,包括100份聚碳酸酯树脂、0.15-1.5份的复配组分;所述的复配组分为受阻酚芳烃衍生物、磷酸猝灭剂、呋喃酮衍生物的复配,其中,以复配组分的总重量计,受阻酚芳烃衍生物所占重量百分比为5-15wt%;磷酸猝灭剂所占重量百分比 为10-30wt%;呋喃酮衍生物所占重量百分比为55-85wt%。
所述的受阻酚芳烃衍生物选自β-(4-羟基-3,5-二叔丁基苯基)丙酸正十八碳醇酯,四〔甲基-(3,5-二叔丁基-4-羟基苯基)丙酸〕季戊四醇酯、三乙二醇醚-二(3-叔丁基-4-羟基-甲基苯基)丙酸酯中的至少一种。
优选的,受阻酚芳烃衍生物选自三乙二醇醚-二(3-叔丁基-4-羟基-甲基苯基)丙酸酯。
所述的磷酸猝灭剂选自三(2,4-二叔丁基苯基)亚磷酸酯、双十八烷基季戊四醇双亚磷酸酯、双(2,4-二叔丁基)季戊四醇二亚磷酸酯中的至少一种。
优选的,磷酸猝灭剂选自双(2,4-二叔丁基)季戊四醇二亚磷酸酯。
所述的呋喃酮衍生物选自二甲苯基二丁基苯并呋喃酮。
优选的,以复配组分的总重量计,受阻酚芳烃衍生物所占重量百分比为7-13wt%;磷酸猝灭剂所占重量百分比为15-25wt%;呋喃酮衍生物所占重量百分比为62-78wt%。
含量优选的,所述的复配组分的量为0.3-0.9份。当复配组分的添加量达到0.3份后即可得到很好的脱模性和成型性,当达到0.9份时再续添加则脱模力提升不明显。
脱模力指将塑件从型芯上脱出时所需克服的阻力,示意图见下说明书附图1。
脱模力计算公式:F脱=f×P×A
f为模芯与制件间的摩擦系数
P为接触压力
A为模芯与制件的接触面积
通过测量模芯上移除圆柱筒所需的力来表征脱模力。
适用于注塑成型加工的聚碳酸酯树脂的重均分子量是19000-35000。
按重量份计,还包括0-30份的阻燃剂;所述的阻燃剂选自C1-C16烷基磺酸盐阻燃剂、碳酸盐类阻燃剂、无机磷酸盐阻燃剂、氟-银离子复合物、磷酸酯类阻燃剂中的至少一种;所述的C1-C16烷基磺酸盐阻燃剂选自全氟辛烷磺酸钾、全氟乙烷磺酸四乙基铵、二苯砜磺酸钾中的至少一种;所述的碳酸盐类阻燃剂选自碳酸钠、碳酸钾、碳酸镁、碳酸钙、碳酸钡中的至少一种。
上述的聚碳酸酯组合物的制备方法,包括以下步骤:将各组分混合均匀,后通过双螺杆挤出机挤出造粒,得到聚碳酸酯组合物,其中,螺杆的温度240℃~260℃,转速为400~600rpm。
与现有技术相比,本发明具有如下有益效果:
相比于现有技术中常规的以润滑剂作为主体的脱模体系,本发明通过选用受阻酚芳烃衍 生物、磷酸猝灭剂、呋喃酮衍生物的复配,不仅能够得到良好的抗氧化效果,并且能够取代润滑剂的添加,并且降低了脱模力,提高的注塑成型加工性能。此外,在阻燃聚碳酸酯体系,能够明显提升阻燃性。
图1:脱模力的示意图。
图2:脱模力过大导致制件脱模时出现拉丝、表面凹凸不平等现象。
本发明是通过以下实施例进行更详细描述,但是本发明不受以下实施例的限制。
本发明所使用的原料来源于市售产品:
聚碳酸酯树脂:PC 1300 10NP,重均分子量22000。
阻燃剂:FR2025,3M公司。
受阻酚芳烃衍生物A:β-(4-羟基-3,5-二叔丁基苯基)丙酸正十八碳醇酯;
受阻酚芳烃衍生物B:四〔甲基-(3,5-二叔丁基-4-羟基苯基)丙酸〕季戊四醇酯。
受阻酚芳烃衍生物C:三乙二醇醚-二(3-叔丁基-4-羟基-甲基苯基)丙酸酯。
磷酸猝灭剂A:三(2,4-二叔丁基苯基)亚磷酸酯。
磷酸猝灭剂B:双十八烷基季戊四醇双亚磷酸酯。
磷酸猝灭剂C:双(2,4-二叔丁基)季戊四醇二亚磷酸酯。
呋喃酮衍生物:二甲苯基二丁基苯并呋喃酮。
抗氧剂A:N,N’-双-(3-(3,5-二叔丁基-4-羟基苯基)丙酰基)己二胺。
抗氧剂B:1,3,5-三(3,5-二叔丁基-4-羟基苯基丙酰氧基乙基)异氰尿酸酯。
抗氧剂C:3,9-双[1,1-二甲基-2-[(3-叔丁基-4-羟基-5-甲基苯基)丙酰氧基]乙基]-2,4,8,10-四氧杂螺[5.5]十一烷。
抗氧剂D:1,3,5-三(4-叔丁基-3-羟基-2,6-二甲基苄基)-1,3,5-三嗪-2,4,6-(1H,3H,5H)-三酮。
润滑剂A:GLYCOLUBE-P,龙沙;
润滑剂B:A-C6A,霍尼韦尔;
润滑剂C:MB50-002,道康宁;
实施例和对比例聚碳酸酯组合物的制备方法:将各组分混合均匀,后通过双螺杆挤出机挤出造粒,得到聚碳酸酯组合物,其中,螺杆的温度240℃~260℃,转速为400~600rpm。
各项性能测试方法:
(1)脱模力:本研究主要通过测量模芯上移除圆柱筒所需的力来表征脱模力,制件见附图。
脱模力计算公式:F脱=f*P*A
f为模芯与制件间的摩擦系数
P为接触压力
A为模芯与制件的接触面积
(2)成型性:
采用脱模后的外观和制件形态来评价。
1级:外观无可见银丝,外部未见缩痕,内部未见孔洞;
2级:浇口可见少量银丝,外部未见缩痕,内部未见孔洞;
3级:制件整体可见少量银丝,外部未见缩痕,内部未见孔洞;
4级:制件整体可见少量银丝,外部未见缩痕,内部孔洞<0.5cm;
5级:制件整体可见少量银丝,外部未见缩痕,内部孔洞>0.5cm。
(3)阻燃性:垂直燃烧,测试标准:UL94-2015,样条尺寸:(125±5mm)×(13.0±0.5mm)×(1.5±0.15mm),23±2℃,50±5%RH调节48h,测试步骤:
火焰高度20±1mm,本生灯置于样品下方正中心位置,本生灯管口距样品底端10±1mm,点火时间为10±0.5s,点火10±0.5s后以300mm/s的速度移开本生灯至少150mm,同时开始记录余焰时间t1,余焰停止时应立即点燃10±0.5s,点火10±0.5s后以300mm/sec的速度移开本生灯至少150mm,同时记录余焰时间t2和余燃时间t3。
火焰等级的评定:
| 判定条件 | V-0 | V-1 | V-2 |
| 每个独立的样品燃烧持续时间t1或t2 | ≤10s | ≤30s | ≤30s |
| 对任意处理组的五个样品的总的燃烧持续时间t1+t2 | ≤50s | ≤250s | ≤250s |
| 在第二次火焰施加后,每个独立的样品燃烧持续时间和灼热燃烧时间t2+t3 | ≤30s | ≤60s | ≤60s |
| 任一样品持续燃烧和灼热燃烧是否到夹持样品的夹子处 | 否 | 否 | 否 |
| 燃烧颗粒或滴落物是否引燃脱脂棉 | 否 | 否 | 是 |
表1:实施例1-8聚碳酸酯组合物组分含量(重量份)及测试结果
由实施例1-4可知,复配组分的用量达到0.3份时能将脱模力降低至接近3800,用量达到0.9份时再继续添加脱模力下降放缓。
由实施例1-8可知,磷酸猝灭剂优选双(2,4-二叔丁基)季戊四醇二亚磷酸酯,受阻酚芳烃衍生物优选三乙二醇醚-二(3-叔丁基-4-羟基-甲基苯基)丙酸酯。
表2:实施例9-14聚碳酸酯组合物组分含量(重量份)及测试结果
由实施例9-12可知,优选的配比下脱模力更低。
由实施例13/14和对比例1-6可知,本发明的复配组分还能够提升阻燃性。
表3:对比例1-7聚碳酸酯组合物组分含量(重量份)及测试结果
表4:对比例8-14聚碳酸酯组合物组分含量(重量份)及测试结果
由对比例1-11可知,现有常用的抗氧剂、及复配都不能很好的达到本发明的技术效果。
由对比例12-14可知,常用的润滑剂虽然经常作为脱模剂使用,但是对于材料的成型性提升不足。
Claims (10)
- 一种聚碳酸酯组合物,其特征在于,按重量份计,包括100份聚碳酸酯树脂、0.15-1.5份的复配组分;所述的复配组分为受阻酚芳烃衍生物、磷酸猝灭剂、呋喃酮衍生物的复配;其中,以复配组分的总重量计,受阻酚芳烃衍生物所占重量百分比为5-15wt%;磷酸猝灭剂所占重量百分比为10-30wt%;呋喃酮衍生物所占重量百分比为55-85wt%。
- 根据权利要求1所述的聚碳酸酯组合物,其特征在于,所述的受阻酚芳烃衍生物选自β-(4-羟基-3,5-二叔丁基苯基)丙酸正十八碳醇酯、四〔甲基-(3,5-二叔丁基-4-羟基苯基)丙酸〕季戊四醇酯、三乙二醇醚-二(3-叔丁基-4-羟基-甲基苯基)丙酸酯中的至少一种;优选的,受阻酚芳烃衍生物为三乙二醇醚-二(3-叔丁基-4-羟基-甲基苯基)丙酸酯。
- 根据权利要求1所述的聚碳酸酯组合物,其特征在于,所述的磷酸猝灭剂选自三(2,4-二叔丁基苯基)亚磷酸酯、双十八烷基季戊四醇双亚磷酸酯、双(2,4-二叔丁基)季戊四醇二亚磷酸酯中的至少一种;优选的,磷酸猝灭剂为双(2,4-二叔丁基)季戊四醇二亚磷酸酯。
- 根据权利要求1所述的聚碳酸酯组合物,其特征在于,所述的呋喃酮衍生物为二甲苯基二丁基苯并呋喃酮。
- 根据权利要求1所述的聚碳酸酯组合物,其特征在于,以复配组分的总重量计,受阻酚芳烃衍生物所占重量百分比为7-13wt%;磷酸猝灭剂所占重量百分比为15-25wt%;呋喃酮衍生物所占重量百分比为62-78wt%。
- 根据权利要求1所述的聚碳酸酯组合物,其特征在于,所述的复配组分的重量份为0.3-0.9份。
- 根据权利要求1所述的聚碳酸酯组合物,其特征在于,所述的聚碳酸酯树脂的重均分子量是19000-35000。
- 根据权利要求1所述的聚碳酸酯组合物,其特征在于,按重量份计,还包括0-30份的阻燃剂;所述的阻燃剂选自C1-C16烷基磺酸盐阻燃剂、碳酸盐类阻燃剂、无机磷酸盐阻燃剂、氟-银离子复合物、磷酸酯类阻燃剂中的至少一种;所述的C1-C16烷基磺酸盐阻燃剂选自全氟辛烷磺酸钾、全氟乙烷磺酸四乙基铵、二苯砜磺酸钾中的至少一种;所述的碳酸盐类阻燃剂选自碳酸钠、碳酸钾、碳酸镁、碳酸钙、碳酸钡中的至少一种。
- 权利要求1-8所述的聚碳酸酯组合物的制备方法,其特征在于,包括以下步骤:将各组分混合均匀,后通过双螺杆挤出机挤出造粒,得到聚碳酸酯组合物,其中,螺杆的温度240℃~260℃,转速为400~600rpm。
- 权利要求1-8所述的聚碳酸酯组合物的应用,其特征在于,用于制备表面光滑的制品。
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| CN104497537A (zh) * | 2014-12-26 | 2015-04-08 | 深圳华力兴新材料股份有限公司 | 一种lds用聚碳酸酯组合物及其制备方法 |
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| CN101492566B (zh) * | 2009-03-09 | 2011-11-02 | 佛山市顺德区瑞能科技有限公司 | 一种无卤阻燃聚碳酸酯组合物及其用途 |
| CN101906244A (zh) * | 2010-08-12 | 2010-12-08 | 东莞市信诺橡塑工业有限公司 | 聚碳酸酯组合物及其制备方法 |
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| JP2004331905A (ja) * | 2003-05-12 | 2004-11-25 | Teijin Chem Ltd | 帯電防止性ポリカーボネート樹脂組成物 |
| CN101792585A (zh) * | 2010-03-16 | 2010-08-04 | 广州市番禺区天宇塑料实业有限公司 | 一种阻燃聚碳酸酯组合物及其制备方法 |
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| CN112341784A (zh) * | 2020-11-16 | 2021-02-09 | 金发科技股份有限公司 | 一种聚碳酸酯组合物及其制备方法和应用 |
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